Method of manufacturing semiconductor device, substrate processing apparatus, gas supply system, and recording medium

ABSTRACT

A method of manufacturing a semiconductor device includes alternately performing supplying a first process gas containing silicon and a halogen element to a substrate having a surface on which monocrystalline silicon and an insulation film are exposed and supplying a second process gas containing silicon and not containing a halogen element to the substrate, and supplying a third process gas containing silicon to the substrate, whereby a first silicon film is homo-epitaxially grown on the monocrystalline silicon and a second silicon film differing in crystal structure from the first silicon film is grown on the insulation film.

CROSS-REFERENCE TO RELATED APPLICATION

This application is based upon and claims the benefit of priority fromJapanese Patent Application No. 2014-234401, filed on Nov. 19, 2014, andJapanese Patent Application No. 2015-185891, filed on Sep. 18, 2015, theentire contents of which are incorporated herein by reference.

TECHNICAL FIELD

The present disclosure relates to a method of manufacturing asemiconductor device, a substrate processing apparatus, a gas supplysystem, and a recording medium.

BACKGROUND

As an example of processes of manufacturing a semiconductor device, afilm forming process of forming a silicon film (Si film) on a substratehaving an insulation film exposed in at least a portion of a surfacethereof is often carried out.

SUMMARY

The present disclosure provides some embodiments of a technique capableof improving the quality of a Si film when forming the Si film on asubstrate having an insulation film exposed in at least a portion of asurface thereof.

According to an aspect of the present disclosure, provided is atechnology including alternately performing supplying a first processgas containing silicon and a halogen element to a substrate having asurface on which monocrystalline silicon and an insulation film areexposed and supplying a second process gas containing silicon and notcontaining a halogen element to the substrate, and supplying a thirdprocess gas containing silicon to the substrate, whereby a first siliconfilm is homo-epitaxially grown on the monocrystalline silicon and asecond silicon film differing in crystal structure from the firstsilicon film is grown on the insulation film.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a schematic configuration view of a vertical processingfurnace of a substrate processing apparatus suitably used in oneembodiment of the present disclosure, in which a portion of theprocessing furnace is shown in a vertical cross section.

FIG. 2 is a schematic configuration view of the vertical processingfurnace of the substrate processing apparatus suitably used in oneembodiment of the present disclosure, in which a portion of theprocessing furnace is shown in a cross section taken along line II-II inFIG. 1.

FIG. 3 is a schematic configuration view of a controller of thesubstrate processing apparatus suitably used in one embodiment of thepresent disclosure, in which a control system of the controller is shownin a block diagram.

FIG. 4 is a view illustrating gas supply timings in a film formingsequence according to one embodiment of the present disclosure.

FIG. 5A is a view illustrating a surface structure of a wafer prior tothe start of a parallel seed step, FIG. 5B is a view illustrating asurface structure of a wafer during the progress of a parallel seed stepand after the supply of a DCS gas, FIG. 5C is a view illustrating asurface structure of a wafer during the progress of a parallel seed stepand after the supply of a DS gas, FIG. 5D is a view illustrating asurface structure of a wafer after the completion of a parallel seedstep, FIG. 5E is a view illustrating a surface structure of a waferduring the progress of a CVD film forming step, FIG. 5F is a viewillustrating a surface structure of a wafer after the completion of aCVD film forming step, and FIG. 5G is a view illustrating a surfacestructure of a wafer after the completion of an annealing step.

FIG. 6 is a view illustrating modification 1 of gas supply timings in afilm forming sequence according to one embodiment of the presentdisclosure.

FIG. 7 is a view illustrating modification 2 of gas supply timings in afilm forming sequence according to one embodiment of the presentdisclosure.

FIG. 8 is a view illustrating modification 3 of gas supply timings in afilm forming sequence according to one embodiment of the presentdisclosure.

FIG. 9 is a view illustrating modification 4 of gas supply timings in afilm forming sequence according to one embodiment of the presentdisclosure.

FIG. 10 is a view illustrating modification 5 of gas supply timings in afilm forming sequence according to one embodiment of the presentdisclosure.

FIG. 11 is a view illustrating modification 6 of gas supply timings in afilm forming sequence according to one embodiment of the presentdisclosure.

FIG. 12A is a view illustrating surface structure example 1 of a waferto be processed, FIG. 12B is a view illustrating surface structureexample 2 of a wafer to be processed, FIG. 12C is a view illustratingsurface structure example 3 of a wafer to be processed, and FIG. 12D isa view illustrating surface structure example 4 of a wafer to beprocessed.

FIG. 13A is a TEM image illustrating a cross-sectional structure of asurface of sample 1 which is subjected to a parallel seed process whenforming a Si film, and FIG. 13B is a TEM image illustrating across-sectional structure of a surface of sample 2 which is notsubjected to a parallel seed process when forming a Si film.

FIG. 14A is a schematic configuration view of a processing furnace of asubstrate processing apparatus suitably used in another embodiment ofthe present disclosure, in which a portion of the processing furnace isshown in a vertical cross section, and FIG. 14B is a schematicconfiguration view of a processing furnace of a substrate processingapparatus suitably used in a further embodiment of the presentdisclosure, in which a portion of the processing furnace is shown in avertical cross section.

FIGS. 15A to 15H are views illustrating manufacturing processes of adynamic random access memory (DRAM), respectively.

FIGS. 16A to 16G are views illustrating manufacturing processes of DRAM,respectively.

FIGS. 17A to 17H are views illustrating manufacturing processes of athree-dimensional NAND type flash memory (3DNAND), respectively.

DETAILED DESCRIPTION One Embodiment of the Present Disclosure

One embodiment of the present disclosure will now be described withreference to FIGS. 1 to 3.

(1) Configuration of Substrate Processing Apparatus

As shown in FIG. 1, a processing furnace 202 includes a heater 207 as aheating part (a heating mechanism). The heater 207 has a cylindricalshape and is supported by a heater base (not shown) serving as a supportplate so as to be vertically installed. As will be described later, theheater 207 functions as an activation mechanism (an excitation part)configured to thermally activate (excite) a gas.

A reaction tube 203 constituting a reaction vessel (process vessel) isdisposed inside the heater 207 in a concentric relationship with theheater 207. The reaction tube 203 is made of, e.g., a heat resistantmaterial such as quartz (SiO₂), silicon carbide (SiC) or the like andhas a cylindrical shape with its upper end closed and its lower endopened. A process chamber 201 is formed in a hollow cylindrical portionof the reaction tube 203. The process chamber 201 is configured toaccommodate a plurality of wafers 200 as substrates. The wafers 200 arehorizontally stacked at multiple stages along a vertical direction in aboat 217 which will be described later.

Nozzles 249 a and 249 b are installed in the process chamber 201 topenetrate through a lower sidewall of the reaction tube 203. The nozzles249 a and 249 b are made of, e.g., a heat resistant material such asquartz, SiC or the like. Gas supply pipes 232 a and 232 b arerespectively connected to the nozzles 249 a and 249 b. A gas supply pipe232 c is connected to the gas supply pipe 232 b. In this way, the twonozzles 249 a and 249 b and the three gas supply pipes 232 a to 232 care installed in the reaction tube 203 and are configured to supplyplural kinds of gases into the process chamber 201.

However, the processing furnace 202 of the present embodiment is notlimited to the configuration as described above. For example, a manifoldmade of metal and configured to support the reaction tube 203 may beinstalled under the reaction tube 203. Each of the nozzles may beinstalled to penetrate through a sidewall of the manifold. In this case,an exhaust pipe 231, which will be described later, may be furtherinstalled in the manifold. Alternatively, the exhaust pipe 231 may beinstalled in a lower portion of the reaction tube 203 rather than in themanifold. A furnace opening portion of the processing furnace 202 may bemade of metal and the nozzles or the like may be installed in themetal-made furnace opening portion.

Mass flow controllers (MFC) 241 a to 241 c, which are flow ratecontrollers (flow rate control parts), and valves 243 a to 243 c, whichare opening/closing valves, are sequentially installed in the gas supplypipes 232 a to 232 c from the corresponding upstream sides. Gas supplypipes 232 d and 232 e, which supply an inert gas, are respectivelyconnected to the gas supply pipes 232 a and 232 b at the downstream sideof the valves 243 a and 243 b. MFCs 241 d and 241 e, which are flow ratecontrollers (flow rate control parts), and valves 243 d and 243 e, whichare opening/closing valves, are sequentially installed in the gas supplypipes 232 d and 232 e from the corresponding upstream sides.

The nozzles 249 a and 249 b are respectively connected to end portionsof the gas supply pipes 232 a and 232 b. As shown in FIG. 2, the nozzles249 a and 249 b are disposed in an annular space, when seen in a planeview, between the inner wall of the reaction tube 203 and the wafers 200such that the nozzles 249 a and 249 b extend upward along an arrangementdirection of the wafers 200 from a lower portion of the inner wall ofthe reaction tube 203 to an upper portion thereof. Specifically, thenozzles 249 a and 249 b are installed along a wafer arrangement regionin which the wafers 200 are arranged, in a region that horizontallysurrounds the wafer arrangement region at a side of the waferarrangement region. That is to say, the nozzles 249 a and 249 b arerespectively installed in a perpendicular relationship with the surfaces(flat surfaces) of the wafers 200 at a lateral side of the end portions(peripheral edge portions) of the wafers 200 carried into the processchamber 201. Each of the nozzles 249 a and 249 b is configured as anL-shaped nozzle. A horizontal portion of each of the nozzles 249 a and249 b is installed to penetrate a lower sidewall of the reaction tube203. A vertical portion of each of the nozzles 249 a and 249 b isinstalled to extend upward at least from one end portion of the waferarrangement region toward the other end portion thereof. A plurality ofgas supply holes 250 a and 250 b for supplying gas is respectivelyformed on the side surfaces of the nozzles 249 a and 249 b. Each of thegas supply holes 250 a and 250 b is opened toward the center of thereaction tube 203 to allow the gas to be supplied toward the wafers 200.The gas supply holes 250 a and 250 b may be formed in a plural number soas to span from the lower portion of the reaction tube 203 to the upperportion thereof. The respective gas supply holes 250 a and 250 b mayhave the same opening area. Further, the gas supply holes 250 a and 250b may be formed at a predetermined opening pitch.

As described above, in the present embodiment, a gas is transferredthrough the nozzles 249 a and 249 b, which are disposed in thevertically-elongated annular space when seen in a plane view, i.e., acylindrical space, defined by the inner surface of the side wall of thereaction tube 203 and the end portions (peripheral edge portions) of thewafers 200 arranged within the reaction tube 203. The gas is initiallyinjected into the reaction tube 203, near the wafers 200, through thegas supply holes 250 a and 250 b formed in the nozzles 249 a and 249 b.Accordingly, the gas supplied into the reaction tube 203 mainly flowswithin the reaction tube 203 in a direction parallel to surfaces of thewafers 200, i.e., in a horizontal direction. With this configuration,the gas can be uniformly supplied to the respective wafers 200. Thismakes a thickness of a thin film formed on each of the wafers 200uniform. In addition, the gas flowing on the surfaces of the wafers 200after reaction, i.e., the reacted residual gas, flows toward an exhaustport, i.e., the exhaust pipe 231 which will be described later. The flowdirection of the residual gas is not limited to a vertical direction butmay be appropriately decided depending on a position of the exhaustport.

A first process gas, for example, a gas containing silicon (Si) and ahalogen element, namely a halosilane precursor gas, is supplied from thegas supply pipe 232 a into the process chamber 201 via the MFC 241 a,the valve 243 a and the nozzle 249 a.

The halosilane precursor gas refers to a gaseous halosilane precursor,for example, a gas obtained by vaporizing a halosilane precursor whichremains in a liquid state under a room temperature and an atmosphericpressure, or a halosilane precursor which remains in a gas state under aroom temperature and an atmospheric pressure. The halosilane precursorrefers to a silane precursor having a halogen group. Examples of thehalogen group may include a chloro group, a fluoro group, a bromo groupand an iodine group. That is to say, the halogen group includes ahalogen element such as chlorine (Cl), fluorine (F), bromine (Br),iodine (I) or the like. The halosilane precursor may be said to be onekind of halide. When the term “precursor” is used herein, it may referto “a precursor staying in a liquid state,” “a precursor (precursor gas)staying in a gaseous state,” or both.

As the first process gas, it may be possible to use, e.g., a halosilaneprecursor gas containing Si and Cl, namely a chlorosilane precursor gascontaining silane chloride (a chlorine compound of silicon). As thechlorosilane precursor gas, it may be possible to use, e.g., adichlorosilane (SiH₂Cl₂, abbreviation: DCS) gas containing one Si atom,two Cl atoms and two hydrogen (H) atoms in one molecule (in onemolecular structure).

A dopant gas, namely a gas containing an impurity (a dopant) to be addedto a finally-formed Si film, is supplied from the gas supply pipe 232 ainto the process chamber 201 via the MFC 241 a, the valve 243 a and thenozzle 249 a. As the dopant gas, it may be possible to use a gascontaining one of a Group III element and a Group V element, forexample, a phosphine (PH₃, abbreviation: PH) gas containing onephosphorus (P) atom and three H atoms in one molecule.

A second process gas, for example, a silane precursor gas containing Siand not containing a halogen element, is supplied from the gas supplypipe 232 b into the process chamber 201 via the MFC 241 b, the valve 243b and the nozzle 249 b. As the second process gas, it may be possible touse a hydrogenated silane precursor gas containing hydrogenated silane(hydrogenated silicon), i.e., a hydrogen compound of silicon, forexample, a disilane (Si₂H₆, abbreviation: DS) containing two Si atomsand six H atoms in one molecule and not containing a halogen element.

A third process gas, for example, a silane precursor gas containing Si,is supplied from the gas supply pipe 232 c into the process chamber 201via the MFC 241 c, the valve 243 c, the gas supply pipe 232 b and thenozzle 249 b. As the third process gas, it may be possible to use ahydrogenated silane precursor gas containing hydrogenated silane(hydrogenated silicon), i.e., a hydrogen compound of silicon, forexample, a monosilane (SiH₄, abbreviation: MS) containing one Si atomand four H atoms in one molecule and not containing a halogen element.

An inert gas, for example, a nitrogen (N₂) gas, is supplied from the gassupply pipes 232 d and 232 e into the process chamber 201 via the MFCs241 d and 241 e, the valves 243 d and 243 e, the gas supply pipes 232 aand 232 b, and the nozzles 249 a and 249 b.

In the case of supplying the first process gas from the gas supply pipe232 a, a first process gas supply system is mainly configured by the gassupply pipe 232 a, the MFC 241 a and the valve 243 a. The nozzle 249 amay be included in the first process gas supply system. The firstprocess gas supply system may be referred to as a first precursor gassupply system or a first precursor supply system. In the case ofsupplying the halosilane precursor gas from the gas supply pipe 232 a,the first process gas supply system may be referred to as a halosilaneprecursor gas supply system or a halosilane precursor supply system.

In the case of supplying the dopant gas from the gas supply pipe 232 a,a dopant gas supply system is mainly configured by the gas supply pipe232 a, the MFC 241 a and the valve 243 a. The nozzle 249 a may beincluded in the dopant gas supply system. The dopant gas supply systemmay be referred to as a dopant supply system.

In the case of supplying the second process gas from the gas supply pipe232 b, a second process gas supply system is mainly configured by thegas supply pipe 232 b, the MFC 241 b and the valve 243 b. The nozzle 249b may be included in the second process gas supply system. The secondprocess gas supply system may be referred to as a second precursor gassupply system or a second precursor supply system. In the case ofsupplying the hydrogenated silane precursor gas from the gas supply pipe232 b, the second process gas supply system may be referred to as ahydrogenated silane precursor gas supply system or a hydrogenated silaneprecursor supply system.

In the case of supplying the third process gas from the gas supply pipe232 c, a third process gas supply system is mainly configured by the gassupply pipe 232 c, the MFC 241 c and the valve 243 c. The nozzle 249 bat the downstream side of a connection portion, at which the gas supplypipe 232 b is connected to the gas supply pipe 232 c, may be included inthe third process gas supply system. The third process gas supply systemmay be referred to as a third precursor gas supply system or a thirdprecursor supply system. In the case of supplying the hydrogenatedsilane precursor gas from the gas supply pipe 232 c, the third processgas supply system may be referred to as a hydrogenated silane precursorgas supply system or a hydrogenated silane precursor supply system.

One or all of the first process gas supply system, the second processgas supply system and the third process gas supply system may bereferred to as a process gas supply system or a film forming gas supplysystem. The dopant gas supply system may be included in the film forminggas supply system (the process gas supply system).

An inert gas supply system is mainly configured by the gas supply pipes232 d and 232 e, the MFCs 241 d and 241 e, and the valves 243 d and 243e. The inert gas supply system may be referred to as a purge gas supplysystem, a dilution gas supply system or a carrier gas supply system.

One or all of the various gas supply systems described above may beconfigured as an integrated gas supply system 248 in which the valves243 a to 243 e, the MFCs 241 a to 241 e, and the like are integrated.The integrated gas supply system 248 is configured to be controlled by acontroller 121 described later, which is connected to the respective gassupply pipes 232 a to 232 e to control the supplying operation ofvarious kinds of gases into the gas supply pipes 232 a to 232 e, i.e.,the opening/closing operation of the valves 243 a to 243 e or the flowrate adjusting operation by the MFCs 241 a to 241 e. The integrated gassupply system 248 is formed in an integral type or split type integratedunits, so that attachment/detachment for the gas supply pipes 232 a to232 e or the like can be performed using the integrated unit as a unitand maintenance, replacement, extension or the like, of the gas supplysystem can be conducted using the integrated unit as a unit. The variousgas supply systems described above may be referred to as a gas supplyunit, a gas supply system, and a gas supply part, respectively.

An exhaust pipe 231 for exhausting an internal atmosphere of the processchamber 201 is installed in the reaction tube 203. A vacuum exhaustdevice, e.g., a vacuum pump 246, is connected to the exhaust pipe 231via a pressure sensor 245, which is a pressure detector (pressuredetecting part) for detecting an internal pressure of the processchamber 201, and an Auto Pressure Controller (APC) valve 244, which is apressure regulator (pressure regulating part). The APC valve 244 isconfigured to perform or stop vacuum exhaust in the process chamber 201by opening or closing the valve while actuating the vacuum pump 246 andis also configured to regulate the internal pressure of the processchamber 201 by adjusting an opening degree of the valve pursuant topressure information detected by the pressure sensor 245 while actuatingthe vacuum pump 246. An exhaust system is mainly configured by theexhaust pipe 231, the APC valve 244, and the pressure sensor 245. Thevacuum pump 246 may be included in the exhaust system.

A seal cap 219, which serves as a furnace opening cover configured tohermetically seal a lower end opening of the reaction tube 203, isinstalled under the reaction tube 203. The seal cap 219 is configured tomake contact with the lower end of the reaction tube 203 at a lower sidein the vertical direction. The seal cap 219 is made of metal such as,e.g., stainless steel or the like, and is formed into a disc shape. AnO-ring 220, which is a seal member making contact with the lower endportion of the reaction tube 203, is installed on an upper surface ofthe seal cap 219. A rotary mechanism 267 configured to rotate a boat217, which will be described later is installed at a side of the sealcap 219 apposite to the process chamber 201. A rotary shaft 255 of therotary mechanism 267, which penetrates through the seal cap 219, isconnected to the boat 217. The rotary mechanism 267 is configured torotate the wafers 200 by rotating the boat 217. The seal cap 219 isconfigured to be vertically moved up and down by a boat elevator 115which is an elevator mechanism vertically installed outside the reactiontube 203. The boat elevator 115 is configured to load and unload theboat 217 into and from the process chamber 201 by moving the seal cap219 up and down. As such, the boat elevator 115 is configured as atransfer device (transfer mechanism) which transfers the boat 217,ultimately, the wafers 200, into and out of the process chamber 201.

The boat 217 serving as a substrate support is configured to support aplurality of wafers 200, e.g., 25 to 200 wafers, in such a state thatthe wafers 200 are arranged in a horizontal posture and in multiplestages along a vertical direction, with the centers of the wafers 200concentrically aligned, to be spaced-apart from one another. The boat217 is made of heat resistant material such as quartz or SiC. Heatinsulating plates 218 made of heat resistant material such as quartz orSiC are installed below the boat 217 in a horizontal posture and inmultiple stages. With this configuration, it is hard for heat generatedfrom the heater 207 to be transferred to the seal cap 219. However, thepresent embodiment is not limited to the above-described configuration.For example, instead of installing the heat insulating plates 218 belowthe boat 217, a heat insulating tube as a tubular member made of heatresistant material such as quartz or SiC may be installed below the boat217.

A temperature sensor 263 serving as a temperature detector is installedin the reaction tube 203. Based on temperature information detected bythe temperature sensor 263, a state of supplying electronic power to theheater 207 is adjusted such that the interior of the process chamber 201has a desired or specified temperature distribution. Similar to thenozzles 249 a and 249 b, the temperature sensor 263 is formed in anL-shape. The temperature sensor 263 is installed along the inner wall ofthe reaction tube 203.

As illustrated in FIG. 3, a controller 121, which is a control part(control means), may be configured as a computer including a centralprocessing unit (CPU) 121 a, a random access memory (RAM) 121 b, amemory device 121 c, and an I/O port 121 d. The RAM 121 b, the memorydevice 121 c and the I/O port 121 d are configured to exchange data withthe CPU 121 a via an internal bus 121 e. An input/output device 122formed of, e.g., a touch panel or the like, is connected to thecontroller 121.

The memory device 121 c is configured with, for example, a flash memory,a hard disc drive (HDD), or the like. A control program for controllingoperations of a substrate processing apparatus or a process recipe, inwhich a sequence or condition for processing a substrate to be describedlater is written, is readably stored in the memory device 121 c. Also,the process recipe functions as a program for the controller 121 toexecute each sequence in the substrate processing procedure, which willbe described later, to obtain a predetermined result. Hereinafter, sucha process recipe or control program may be generally referred to as “aprogram.” Further, the process recipe may be simply referred to as “arecipe.” Also, when the term “program” is used herein, it may indicate acase of including only a recipe, a case of including only a controlprogram, or a case of including both a recipe and a control program. Inaddition, the RAM 121 b is configured as a memory area (work area) inwhich a program or data read by the CPU 121 a is temporarily stored.

The I/O port 121 d is connected to the MFCs 241 a to 241 e, the valves243 a to 243 e, the pressure sensor 245, the APC valve 244, the vacuumpump 246, the heater 207, the temperature sensor 263, the rotarymechanism 267, the boat elevator 115, and the like.

The CPU 121 a is configured to read and execute the control program fromthe memory device 121 c. The CPU 121 a also reads the recipe from thememory device 121 c according to an input of an operation command fromthe input/output device 122. In addition, the CPU 121 a is configured tocontrol the flow rate adjusting operation of various kinds of gases bythe MFCs 241 a to 241 e, the opening/closing operation of the valves 243a to 243 e, the opening/closing operation of the APC valve 244, thepressure regulating operation performed by the APC valve 244 based onthe pressure sensor 245, the start/stop operation of the vacuum pump246, the temperature adjusting operation performed by the heater 207based on the temperature sensor 263, the operation of rotating the boat217 with the rotary mechanism 267 and adjusting the rotation speed ofthe boat 217, the operation of moving the boat 217 up and down with theboat elevator 115, and the like, according to contents of the readrecipe.

Moreover, the controller 121 may be configured by installing theabove-described program stored in an external memory device 123 (forexample, a magnetic tape, a magnetic disc such as a flexible disc or ahard disc, an optical disc such as a CD or DVD, a magneto-optical discsuch as an MO, a semiconductor memory such as a USB memory or a memorycard) on the computer. The memory device 121 c or the external memorydevice 123 is configured as a non-transitory computer-readable recordingmedium. Hereinafter, these will be simply collectively referred to as “arecording medium.” In addition, when the term “recording medium” is usedin the subject specification, it may indicate a case of including onlythe memory device 121 c, a case of including only the external memorydevice 123, or a case of including both the memory device 121 c and theexternal memory device 123. The program may be supplied to the computerusing communication means such as the Internet or a dedicated line,rather than through the external memory device.

(2) Substrate Processing Process

An example of a sequence for forming a Si film on a substrate andthermally treating the Si film, which is one of the procedures formanufacturing a semiconductor device, by using the above-describedsubstrate processing apparatus, will be described below with referenceto FIGS. 4 and 5A to 5G. In the following descriptions, the operationsof the respective units or parts constituting the substrate processingapparatus are controlled by the controller 121.

In a film forming sequence illustrated in FIG. 4, a first Si film 200 eis caused to homo-epitaxially grow on monocrystalline Si and a second Sifilm 200 g differing in crystal structure from the first Si film 200 eis caused to grow on an insulation film 200 a, by performing:

a step (parallel seed step) of alternately performing Step 1 ofsupplying a DCS gas as a first process gas to a wafer 200 as a substratehaving a surface on which the monocrystalline Si and the insulation film200 a are exposed and Step 2 of supplying a DS gas as a second processgas to the wafer 200; and

a step (CVD film forming step) of supplying an MS gas as a third processgas to the wafer 200.

That is to say, in a film forming sequence illustrated in FIG. 4, alaminated structure (laminated film) including the first Si film 200 eand the second Si film 200 g formed on the first Si film 200 e is formedon the monocrystalline Si by using three kinds of silane precursor gases(triple Si sources). In the following descriptions, the laminated filmmay be simply referred to as a Si film.

Thereafter, a step (annealing step) of making a portion of the second Sifilm 200 g which makes contact with the first Si film 200 e (ahomo-epitaxial Si film) homo-epitaxial is performed by thermallytreating (annealing) the Si film including the first Si film 200 e andthe second Si film 200 g formed on the first Si film 200 e.

In the subject specification, for the sake of convenience, the filmforming sequence described above may be denoted as follows. Furthermore,the annealing is often referred to as ANL.[(DCS→DS)×n→MS]→ANL

Si

As used herein, the term “wafer” may refer to “a wafer itself” or “awafer and a laminated body (a collected body) of predetermined layers orfilms formed on a surface of the wafer” (i.e., a wafer includingpredetermined layers or films formed on its surface may be referred toas a wafer). In addition, as used herein, the phrase “a surface of awafer” may refer to “a surface (exposed surface) of a wafer itself” or“a surface of a predetermined layer or film formed on a wafer, namely anuppermost surface of the wafer, which is a laminated body.”

As such, as used herein, the sentence “a predetermined gas is suppliedto a wafer” may mean that “a predetermined gas is directly supplied to asurface (exposed surface) of a wafer itself” or that “a predeterminedgas is supplied to a layer or film formed on a wafer, namely on anuppermost surface of a wafer as a laminated body.” Also, as used herein,the sentence “a predetermined layer (or film) is formed on a wafer” maymean that “a predetermined layer (or film) is directly formed on asurface (exposed surface) of a wafer itself” or that “a predeterminedlayer (or film) is focused on a layer or film formed on a wafer, namelyon an uppermost surface of a wafer as a laminated body.”

In addition, the term “substrate” as used herein may be synonymous withthe term “wafer.”

(Wafer Charging and Boat Loading)

A plurality of wafers 200 is charged on the boat 217 (wafer charging).Thereafter, as illustrated in FIG. 1, the boat 217 charged with theplurality of wafers 200 is lifted up by the boat elevator 115 and isloaded into the process chamber 201 (boat loading). In this state, theseal cap 219 seals the lower end of the reaction tube 203 through theO-ring 220.

As the wafer 200, it may be possible to use, e.g., a Si substratecomposed of monocrystalline Si or a substrate having a surface on whicha monocrystalline Si film is formed. As illustrated as apartially-enlarged view in FIG. 12A, an insulation film 200 a, e.g., asilicon oxide film (SiO₂ film) (hereinafter also referred to as a SiOfilm), is formed in advance in a portion of the surface of the wafer200. That is to say, the surface of the wafer 200 stays in such a statethat the monocrystalline Si and the insulation film 200 a are exposed.The insulation film 200 a may be, in addition to the SiO film, aSi-based insulation film such as a silicon nitride film (SiN film), asilicon carbide film (SiC film), a silicon carbonitride film (SiCNfilm), a silicon oxynitride film (SiON film), a silicon oxycarbide film(SiOC film), a silicon oxycarbonitride film (SiOCN film), a siliconboronitride film (SiBN film), a silicon borocarbonitride film (SiBCNfilm) or the like, or a metal-based insulation film such as an aluminumoxide film (AlO film), a hafnium oxide film (HfO film), a zirconiumoxide film (ZrO film), a titanium oxide film (TiO film) or the like.That is to say, the insulation film 200 a may be a high-k film(high-permittivity insulating film) such as an MO film, a ZrO film orthe like, or may be a low-k film (low-permittivity insulating film) suchas an SiOCN film, an SiOC film, an SiBN film, an SiBCN film or the like.

FIGS. 5A to 5G illustrate a case where a wafer 200 having a surfacestructure illustrated in FIG. 12A is processed, namely a case where awafer 200 having a recess formed on the surface thereof with a bottomportion of the recess composed of monocrystalline Si and a side portionand a top portion of the recess composed of an insulation film (SiOfilm) 200 a is processed. For the sake of convenience, FIGS. 5A to 5Gillustrate the surface of the wafer 200 in partially-enlarged views.Prior to carrying the wafer 200 into the process chamber 201, thesurface of the wafer 200 is cleaned in advance by hydrogen fluoride (HF)or the like. However, the surface of the wafer 200 is temporarilyexposed to the atmosphere until the wafer 200 is carried into theprocess chamber 201 after the cleaning. For that reason, as illustratedin FIG. 5A, a natural oxide film (SiO film) 200 b is formed in at leasta portion of the surface of the wafer 200 carried into the processchamber 201. The natural oxide film 200 b may be formed so as tosparsely (in an island shape) cover the bottom portion of the recess,namely a portion of the exposed monocrystalline Si, or may be formed soas to continuously (in a non-island shape) cover the entire region ofthe exposed monocrystalline Si.

(Pressure Regulation and Temperature Adjustment)

The interior of the process chamber 201, namely the space in which thewafers 200 exist is vacuum-exhausted (pressure-reducingly exhausted) bythe vacuum pump 246 so as to have a desired or specified pressure(desired or specified vacuum level). In this operation, the internalpressure of the process chamber 201 is measured by the pressure sensor245. The APC valve 244 is feedback-controlled based on the measuredpressure information. The vacuum pump 246 may be continuously activatedat least until the processing of the wafers 200 is completed. The wafers200 in the process chamber 201 are heated by the heater 207 to a desiredor specified temperature. In this operation, the state of supplyingelectric power to the heater 207 is feedback-controlled based on thetemperature information detected by the temperature sensor 263 such thatthe interior of the process chamber 201 reaches a desired or specifiedtemperature distribution. In addition, the heating of the interior ofthe process chamber 201 by the heater 207 may be continuously performedat least until the processing of the wafers 200 is completed. The boat217 and the wafers 200 begin to be rotated by the rotary mechanism 267.The rotation of the boat 217 and the wafers 200 by the rotary mechanism267 may be continuously performed at least until the processing of thewafers 200 is completed.

(Parallel Seed Step)

Next, the following two steps, i.e., Steps 1 and 2, are sequentiallyperformed.

[Step 1]

(DCS Gas Supply)

At this step, a DCS gas is supplied to the wafer 200 existing within theprocess chamber 201.

The valve 243 a is opened to flow a DCS gas through the gas supply pipe232 a. The DCS gas is flow rate-adjusted by the MFC 241 a. The DCS gasis supplied into the process chamber 201 via the nozzle 249 a and isexhausted from the exhaust pipe 231. At this time, the DCS gas issupplied to the wafer 200. At the same time, the valve 243 d is openedto flow a N₂ gas through the gas supply pipe 232 d. The N₂ gas is flowrate-adjusted by the MFC 241 d. The flow rate-adjusted N₂ gas issupplied into the process chamber 201 together with the DCS gas and isexhausted from the exhaust pipe 231. In order to prevent the DCS gasfrom infiltrating into the nozzle 249 b, the valve 243 e is opened toflow the N₂ gas through the gas supply pipe 232 e. The N₂ gas issupplied into the process chamber 201 through the gas supply pipe 232 band the nozzle 249 b and is exhausted from the exhaust pipe 231.

By supplying the DCS gas to the wafer 200, it is possible to perform thefollowing processes and to change the surface state of the wafer 200 tothe state illustrated in FIG. 5B.

First, in the bottom portion of the recess, namely on themonocrystalline Si, due to the supply of DCS which contains halogen (Cl)exhibiting large electronegativity, oxygen (O) of the natural oxide film200 b formed on the surface of the monocrystalline Si and Cl of DCS pullagainst each other. It is therefore possible to break Si—O bondscontained in the natural oxide film 200 b. Thus, the bonds of Siexisting on the surface of the monocrystalline Si become free. That isto say, it is possible to generate dangling bonds of covalent bonds ofSi on the surface of the monocrystalline Si. This provides anenvironment in which the later-described homo-epitaxial growth easilygoes ahead. In the bottom portion of the recess, due to the generationof the aforementioned reaction, the natural oxide film 200 b formed onthe surface of the monocrystalline Si is removed. That is to say, theDCS gas acts as a cleaning gas which removes the natural oxide film 200b from the surface of the monocrystalline Si.

In the side portion and the top portion of the recess, namely on theinsulation film (SiO film) 200 a, due to the supply of DCS whichcontains halogen (Cl) exhibiting large electronegativity, O of thesurface of the insulation film 200 a and Cl of DCS pull against eachother. It is therefore possible to break Si—O bonds contained in theinsulation film 200 a. This makes it possible to form dangling bonds ofSi, i.e., Si adsorption sites, on the surface of the insulation film 200a. Essentially, dangling bonds of Si do not exist on the insulation film200 a such as a SiO film or the like. Even if dangling bonds of Siexist, the number of dangling bonds is not so large. For that reason,even if Step 2 of supplying a DS gas to the wafer 200 is performed inthis state, Si nuclei do not grow on the surface of the insulation film200 a. Even if Si nuclei grow, the growth of the Si nuclei occursrandomly (in an island shape).

(Residual Gas Removal)

If there is provided an environment in which homo-epitaxial growtheasily occur in the bottom portion of the recess and if Si adsorptionsites are formed in the side portion and the top portion of the recess,the valve 243 a is closed to stop the supply of the DCS gas. At thistime, the APC valve 244 is kept opened and the interior of the processchamber 201 is evacuated by the vacuum pump 246. The gas remainingwithin the process chamber 201, which has not reacted or which hascontributed to the aforementioned reaction, is removed from the interiorof the process chamber 201. At this time, the valves 243 d and 243 e arekept opened to continuously supply the N₂ gas into the process chamber201. The N₂ gas acts as a purge gas. This makes it possible toeffectively remove the gas remaining within the process chamber 201 fromthe interior of the process chamber 201.

In this case, the gas remaining within the process chamber 201 may notbe completely removed and the interior of the process chamber 201 maynot be completely purged. If the amount of the gas remaining within theprocess chamber 201 is small, an adverse effect may not be generated atStep 2 which will be subsequently performed. The flow rate of the N₂ gassupplied into the process chamber 201 need not be made large. Forexample, an amount of the N₂ gas to be supplied into the process chamber201 may be set substantially equal to the volume of the reaction tube203 (the process chamber 201) such that a purge operation is performedwithout causing an adverse effect at Step 2. As such, by not completelypurging the interior of the process chamber 201, it is possible toshorten the purge time and to improve the throughput. It is alsopossible to suppress the consumption of the N₂ gas to a necessaryminimum level.

[Step 2]

(DS Gas Supply)

After Step 1 is completed, a DS gas is supplied to the wafer 200existing within the process chamber 201.

At this step, the opening/closing control of the valves 243 b, 243 d and243 e is performed in a procedure similar to the procedure of theopening/closing control of the valve 243 a, 243 d and 243 e at Step 1.The DS gas flowing through the gas supply pipe 232 b isflow-rate-adjusted by the MFC 241 b. The DS gas is supplied into theprocess chamber 201 through the nozzle 249 b and is exhausted from theexhaust pipe 231. At this time, the DS gas is supplied to the wafer 200.

By supplying the DS gas to the wafer 200, it is possible to perform thefollowing processes and to change the surface state of the wafer 200 tothe state illustrated in FIG. 5C, namely the state in which two kinds ofseeds are formed in parallel.

First, in the bottom portion of the recess, namely on themonocrystalline Si, Si contained in DS is bonded to dangling bonds of Siformed by performing Step 1. This enables Si crystals to growepitaxially (in gas phase epitaxy) on the monocrystalline Si. Since thecrystals serving as a base and the crystals grown on these crystals aremade of the same material (Si), the growth becomes homo-epitaxialgrowth. In the homo-epitaxial growth, on the crystals serving as a base,crystals having the same lattice constant as that of the crystalsserving as a base and made of the same material as the crystals servingas a base grow in the same crystal orientation. For that reason, in thehomo-epitaxial growth, it is possible to obtain less-defectivehigh-quality crystals as compared with hetero-epitaxial growth in whichthe crystals serving as a base and the crystals grown on these crystalsare made of mutually-different materials. The nucleus (or the film)formed at this time may be regarded as a seed (a first seed) 200 c of afirst Si film (an epitaxial Si film) 200 e which will be describedlater.

In the side portion and the top portion of the recess, namely on theinsulation film 200 a, it is possible to allow Si contained DS to beadsorbed to the adsorption sites formed by performing Step 1. Thecrystal structure of the nucleus formed as a result of adsorption of Sito the adsorption sites becomes an amorphous, a poly (polycrystal) or amixture of the amorphous and the poly. The nucleus formed at this timemay be regarded as a seed (a second seed) 200 d of a second Si film 200g which will be described later.

(Residual Gas Removal)

If the formation of the first seed 200 c and the second seed 200 d,namely, the formation of the two kinds of seeds (a parallel seedprocess), is completed, the valve 243 b is closed to stop the supply ofthe DS gas. Then, the gas remaining within the process chamber 201,which has not reacted or which has contributed to the aforementionedreaction, or the reaction byproduct is removed from the interior of theprocess chamber 201 by the processing procedures similar to those ofStep 1. At this time, similar to Step 1, the vas or the like remainingwithin the process chamber 201 may not be completely removed.

[Performing a Predetermined Number of Times]

At the parallel seed step, a cycle which alternately, i.e.,non-synchronously or non-simultaneously performs Steps 1 and 2 describedabove is executed a predetermined number of times (once or more). Byperforming the parallel seed step, it is possible to perform thefollowing processes and to change the surface state of the wafer 200 tothe state illustrated in FIG. 5D.

First, in the bottom portion of the recess, namely on themonocrystalline Si, it is possible to form a first Si film 200 e. Thefirst Si film 200 e is formed by allowing a Si crystal tohomo-epitaxially grow using, as a nucleus, the first seed 200 c formedon the monocrystalline Si. The crystal structure of the first Si film200 e becomes a single crystal which inherits the crystallinity of thebase. That is to say, the first Si film 200 e becomes a monocrystallineSi film (an epitaxial Si film) which is made of the same material as themonocrystalline Si of the base and which has the same lattice constantand the same crystal orientation as those of the monocrystalline Si ofthe base. The first Si film 200 e formed at the parallel seed step maybe regarded as a seed layer. In this case, the seed layer is composed ofan epitaxial Si layer. The seed layer composed of the epitaxial Si layermay be referred to as a first seed layer.

In the side portion and the top portion of the recess, namely on theinsulation film 200 a, it is possible to form a seed layer 200 f. Theseed layer 200 f is formed by allowing the second seed 200 d to grow onthe insulation film 200 a at a high density. The seed layer 200 fbecomes a layer which densely covers the surface of the insulation film200 a. The crystal structure of the seed layer 200 f becomes anamorphous, a poly or a mixture of the amorphous and the poly. That is tosay, the seed layer 200 f becomes an amorphous Si layer, a poly Si layeror an amorphous/poly-mixed Si layer. The seed layer 200 f may bereferred to as a second seed layer.

As described above, at the parallel seed step, the first seed layer (theepitaxial Si layer) and the second seed layer (the amorphous Si layer,the poly Si layer or the amorphous/poly-mixed Si layer) are formed inparallel on the monocrystalline Si and the insulation film 200 a,respectively. That is to say, at the parallel seed step, two kinds of Siseed layers differing in crystal structure from each other are formed inparallel. This is why this step is called the parallel seed step.

[Processing Conditions of Parallel Seed Step]

At Step 1, the supply flow rate of the DCS gas controlled by the MFC 241a is set to fall within a range of, e.g., 10 to 1,000 sccm, and in someembodiments, 10 to 500 sccm. The time period for supplying the DCS gasto the wafer 200, namely the gas supply time (irradiation time), is setto fall within a range of, e.g., 0.5 to 10 minutes, and in someembodiments, 1 to 5 minutes.

At Step 2, the supply flow rate of the DS gas controlled by the MFC 241b is set to fall within a range of, e.g., 10 to 1,000 sccm, and in someembodiments, 10 to 500 sccm. The time period for supplying the DS gas tothe wafer 200, namely the gas supply time (irradiation time), is set tofall within a range of, e.g., 0.5 to 10 minutes, and in someembodiments, 1 to 5 minutes.

At Steps 1 and 2, the supply flow rate of the N₂ gas controlled by theMFCs 241 d and 241 e is set to fall within a range of e.g., 100 to10,000 sccm.

At Steps 1 and 2, the internal pressure of the process chamber 201 isset to fall within a range of, e.g., 1 to 1,000 Pa, and in someembodiments, 1 to 100 Pa.

At Steps 1 and 2, the temperature of the heater 207 is set such that thetemperature of the wafer 200 becomes a temperature (a first temperature)which falls within a range of, e.g., 350 to 450 degrees C., and in someembodiments, 370 to 390 degrees C.

If the temperature of the wafer 200 is less than 350 degrees C., DSsupplied at Step 2 is hardly decomposed. Thus, it is sometimes difficultto form the first seed 200 c and the second seed 200 d, namely the firstSi film 200 e and the seed layer 200 f, on the wafer 200. Theaforementioned problem may be solved by setting the temperature of thewafer 200 at 350 degrees C. or more. By setting the temperature of thewafer 200 at 370 degrees C. or more, it is possible to promotedecomposition of DS supplied at Step 2 and to reliably generate thebreaking reaction of the aforementioned Si—O bonds using DCS supplied atStep 1. That is to say, it is possible to reliably provide anenvironment, in which homo-epitaxial growth easily occurs in the bottomportion of the recess, and to reliably perform the formation of the Siadsorption sites in the side portion and the top portion of the recess.It is also possible to reliably perform the formation of the first seed200 c and the second seed 200 d, namely the formation of the first Sifilm 200 e and the seed layer 200 f, on the wafer 200.

If the temperature of the wafer 200 exceeds 450 degrees C., there may bea case where Si contained in DCS supplied at Step 1 is deposited on thewafer 200. In this case, Si is deposited before the natural oxide filmis removed from the surface of the monocrystalline Si. For that reason,homo-epitaxial growth does not occur on the monocrystalline Si (thenatural oxide film). An amorphous Si film or a poly Si film grows on themonocrystalline Si (the natural oxide film). Furthermore, if thetemperature of the wafer 200 exceeds 450 degrees C., there may be a casewhere it becomes difficult to generate the breaking reaction of theaforementioned Si—O bonds using DCS. As a result, it is sometimesdifficult to form the first seed 200 c and the second seed 200 d, namelythe first Si film 200 e and the seed layer 200 f, on the wafer 200. Theaforementioned problem may be solved by setting the temperature of thewafer 200 at 450 degrees C. or less. By setting the temperature of thewafer 200 at 390 degrees C. or less, it becomes possible to reliablygenerate the breaking reaction of the aforementioned Si—O bonds usingDCS, while reliably suppressing the deposition of Si contained in DCS onthe wafer 200. That is to say, it is possible to reliably provide anenvironment, in which homo-epitaxial growth easily occurs in the bottomportion of the recess, and to reliably perform the formation of the Siadsorption sites in the side portion and the top portion of the recess.This makes it possible to reliably perforin the formation of the firstseed 200 c and the second seed 200 d, namely the formation of the firstSi film 200 e and the seed layer 200 f, on the wafer 200.

Accordingly, the temperature of the wafer 200 may be set to fall withina range of, e.g., 350 to 450 degrees C., and in some embodiments, 370 to390 degrees C.

The number of execution times of the cycle which alternately performsSteps 1 and 2 is set to fall within a range of e.g., 1 to 20 times, andin some embodiments, 1 to 10 times. The thickness of the first Si film200 e thus formed and the thickness of the seed layer 200 f arerespectively set to fall within a range of, e.g., 1 to 50 Å, and in someembodiments, 5 to 20 Å.

As the first process gas, in addition to the DCS gas, it may be possibleto use a chlorosilane precursor gas such as a monochlorosilane (SiH₃CL,abbreviation: MCS) gas, a tetrachlorosilane, i.e., silicon tetrachloride(SiCl₄, abbreviation: STC) gas, a trichlorosilane (SiHCl₃, abbreviation:TCS) gas, a hexachlorodisilane (Si₂Cl₆, abbreviation: HCDS) gas or thelike. At Step 1, in order to promote the breaking reaction of theaforementioned Si—O bonds while suppressing the deposition of Si on thewafer 200, it may be possible to use, as the first process gas, ahalosilane precursor gas which has a small number of Si atoms containedin one molecule and a large number of halogen elements (Cl atoms, etc.)contained in one molecule. At Step 1, in order to appropriately suppressthe breaking reaction of the aforementioned Si—O bonds, it may bepossible to use a halosilane precursor gas which has a small number ofhalogen elements (Cl, etc.) contained in one molecule.

As the second process gas, in addition to the DS gas, it may be possibleto use a halogen-element-free silane precursor gas such as an MS gas, atrisilane (Si₃H₈, abbreviation: TS) gas or the like.

As the inert gas, in addition to the N₂ gas, it may be possible to use,e.g., a noble gas such as an Ar gas, a He gas, a Ne gas, a Xe gas or thelike.

(CVD Film Forming Step)

After forming the first Si film 200 e and the seed layer 200 f, an MSgas and a PH gas are supplied to the wafer 200 existing within theprocess chamber 201.

At this step, the opening/closing control of the valves 243 c, 243 d and243 e is performed in a procedure similar to the procedure of theopening/closing control of the valves 243 a, 243 d and 243 e at Step 1.The MS gas flowing through the gas supply pipe 232 c isflow-rate-controlled by the MFC 241 c. The MS gas is supplied into theprocess chamber 201 through the gas supply pipe 232 b and the nozzle 249b and is exhausted from the exhaust pipe 231. At this time, the valve243 a is opened to allow the PH gas to flow through the gas supply pipe232 a. The PH gas is flow-rate-adjusted by the MFC 241 a. The PH gas issupplied into the process chamber 201 through the nozzle 249 a and isexhausted from the exhaust pipe 231. At this time, the MS gas and the PHgas are collectively and simultaneously supplied to the wafer 200.

By supplying the MS gas and the PH gas to the wafer 200, it is possibleto perform the following processes and to sequentially change thesurface state of the wafer 200 to the states illustrated in FIGS. 5E and5F.

First, as illustrated in FIG. 5E, in the bottom portion of the recess,namely on the monocrystalline Si, the first Si film 200 e formed byperforming the parallel seed step may be caused to grow homo-epitaxially(in gas phase epitaxy). That is, it is possible to additionally grow anepitaxial Si film having the same crystal structure as the first Si film200 e on the first Si film 200 e shown in FIG. 15D. By supplying the PHgas together with the MS gas, it is possible to add a P component as adopant into the first Si film 200 e.

Furthermore, as illustrated in FIG. 5E, in the side portion and the topportion of the recess, namely on the insulation film 200 a, it ispossible to form the second Si film 200 g on the seed layer 200 f formedby performing the parallel seed step. The crystal structure of thesecond Si film 200 g becomes an amorphous, a poly or a mixture of theamorphous and the poly. That is to say, the second Si film 200 g becomesan amorphous Si layer, a poly Si layer or an amorphous/poly-mixed Silayer. Since the seed layer 200 f is very thin and is identical incrystal structure and material with the second Si film 200 g, the seedlayer 200 f may be included in the second Si film 200 g. By supplyingthe PH gas together with the MS gas, it is possible to add a P componentas a dopant into the second Si film 200 g.

By continuously performing the aforementioned processes, the growth ofthe first Si film 200 e may be stopped by the growth of the second Sifilm 200 g. That is to say, as illustrated in FIG. 5F, the top portionof the first Si film 200 e may be covered with the second Si film 200 ggrown from the side portion of the recess, thereby stopping thehomo-epitaxial growth of the first Si film 200 e. In this state, alaminated structure (a laminated film) including the first Si film 200 eand the second Si film 200 g laminated on the first Si film 200 e isformed within the recess, namely on the wafer 200. The interior of therecess is closed by the laminated film, namely embedded with thelaminated film. As described above, in the subject specification, thelaminated film may be simply referred to as a Si film.

After the laminated film is formed, the valves 243 c and 243 a areclosed to stop the supply of the MS gas and the PH gas into the processchamber 201. Then, by the processing procedures similar to those of Step1 described above, the gas remaining within the process chamber 201,which has not reacted or which has contributed to the aforementionedreaction, or the reaction byproduct is removed from the interior of theprocess chamber 201. At this time, similar to Step 1, the gas or thelike remaining within the process chamber 201 may not be completelyremoved.

[Processing Condition of CVD Film Forming Step]

The supply flow rate of the MS gas controlled by the MFC 241 c is set tofall within a range of e.g., 10 to 2,000 sccm, and in some embodiments,500 to 1,000 sccm. The time period for supplying the MS gas to the wafer200, namely the gas supply time (irradiation time), may be appropriatelydecided depending on the thickness of the Si film formed on the wafer200.

The supply flow rate of the PH gas controlled by the MFC 241 a isappropriately decided depending on the specifications of a device formedon the wafer 200. The supply flow rate of the PH gas may be set to fallwithin a range of e.g., 0.1 to 500 sccm, and in some embodiments, 1 to100 sccm. The time period for supplying the PH gas to the wafer 200,namely the gas supply time (irradiation time), may be appropriatelydecided depending on the specifications of a device formed on the wafer200.

The supply flow rates of the N₂ gas controlled by the MFCs 241 d and 241e may be respectively set to fall within a range of, e.g., 100 to 10,000sccm.

The internal pressure of the process chamber 201 is set to fall within arange of, e.g., 1 to 1,000 Pa, and in some embodiments, 1 to 100 Pa.

The temperature of the heater 207 is set such that the temperature ofthe wafer 200 becomes a temperature (a second temperature) equal to orhigher than the aforementioned first temperature. Specifically, thetemperature of the heater 207 is set such that the temperature of thewafer 200 becomes a temperature (a second temperature) which fallswithin a range of e.g., 350 to 650 degrees C., and in some embodiments,400 to 550 degrees C.

If the temperature of the wafer 200 is less than 350 degrees C., the gasmay be hardly decomposed depending on the kind of the third process gas.Consequently, it is sometimes difficult to perform the homo-epitaxialgrowth of the first Si film 200 e or the formation process of the secondSi film 200 g (hereinafter often referred to as a CVD film formingprocess). For example, when the DS gas is used as the third process gas,if the temperature of the wafer 200 is less than 350 degrees C., DS ishardly decomposed. This makes it difficult to perform the aforementionedCVD film forming process. This problem may be solved by setting thetemperature of the wafer 200 at 350 degrees C. or more. Furthermore, ifthe temperature of the wafer 200 is set at 400 degrees C. or more, itbecomes easy to perform the aforementioned CVD film forming process. Forexample, when the DS gas is used as the third process gas, if thetemperature of the wafer 200 is set at 400 degrees C. or more, itbecomes easy to decompose DS. This makes it possible to reliably performthe aforementioned CVD film forming process. Furthermore, when the MSgas is used as the third process gas, if the temperature of the wafer200 is set at 450 degrees C. or more, it becomes easy to decompose MS.This makes it possible to reliably perform the aforementioned CVD filmforming process.

If the temperature of the wafer 200 exceeds 650 degrees C., a CVDreaction becomes too strong (an excessive gas phase reaction isgenerated). Thus, the film thickness uniformity easily deteriorates andis hardly controllable. Furthermore, there is a possibility thatparticles are generated within the process chamber 201. This maysometimes reduce the quality of a laminated film formed on the wafer200. By setting the temperature of the wafer 200 at 650 degrees C. orless, it is possible to generate a proper gas phase reaction. This makesit possible to suppress deterioration of the film thickness uniformityand to control the film thickness uniformity. Moreover, it is possibleto suppress generation of particles within the process chamber 201.Particularly, by setting the temperature of the wafer 200 at 550 degreesC. or less, it becomes easy to secure the film thickness uniformity andto control the film thickness uniformity.

Accordingly, the temperature of the wafer 200 may be set at thetemperature (the second temperature) which falls within a range of e.g.,350 to 650 degrees C., and in some embodiments, 400 to 550 degrees C. Ifthe temperature of the wafer 200 is set at a temperature which fallswithin a range of 350 to 520 degrees C., the second Si film 200 g has astrong tendency to become an amorphous Si film. Furthermore, if thetemperature of the wafer 200 is set at a temperature which falls withina range of 520 to 530 degrees C., the second Si film 200 g has a strongtendency to become an amorphous/poly-mixed Si film. In addition, if thetemperature of the wafer 200 is set at a temperature which falls withina range of 530 to 650 degrees C., the second Si film 200 g has a strongtendency to become a poly Si film. In either case, the first Si film 200e becomes an epitaxial Si film.

The thickness of the first Si film 200 e and the thickness of the secondSi film 200 g grown at the CVD film forming step are appropriatelydecided depending on the specifications of a device formed on the wafer200 and may be, for example, 1 to 5,000 Å.

As the third process gas, in addition to the MS gas, it may be possibleto use the aforementioned halogen-element-free hydrogenated silaneprecursor gas or the aforementioned halosilane precursor gas. From theviewpoint of restraining the halogen element from remaining within thefirst Si film 200 e and the second Si film 200 g, thehalogen-element-free hydrogenated silane precursor gas may be used asthe third process gas. In addition, from the viewpoint of improving thedeposition rate of the first Si film 200 e and the second Si film 200 g,the halosilane precursor gas exhibiting high reactivity may be used asthe third process gas.

As the dopant gas, in addition to the PH gas, it may be possible to usea gas containing a Group V element (P, As, etc.), such as an arsine(AsH₃) gas or the like. Furthermore, as the dopant gas, in addition tothe gas containing a Group V element, it may be possible to use a gascontaining a Group III element (B, etc.), such as a diborane (B₂H₆) gas,a trichloroborane (BCl₃) gas or the like.

As the inert gas, in addition to the N₂ gas, it may be possible to use,e.g., a noble gas such as an Ar gas, a He gas, a Ne gas, a Xe gas or thelike.

(Annealing Step)

After the formation of the first Si film 200 e and the second Si film200 g is completed, the temperature of the heater 207 is appropriatelyadjusted to thermally treat the first Si film 200 e and the second Sifilm 200 g formed on the wafer 200.

This step may be performed in a state in which the valves 243 d and 243e are opened to supply the N₂ gas into the process chamber 201 or astate in which the valves 243 d and 243 e are closed to stop the supplyof the N₂ gas into the process chamber 201. In either case, this step isperformed by closing the valves 243 a to 243 c and stopping the supplyof the silane precursor gas into the process chamber 201.

By performing the annealing step, the laminated film of the first Sifilm 200 e and the second Si film 200 g formed on the wafer 200 may bechanged to the film illustrated in FIG. 5G. That is to say, the portionof the second Si film 200 g (the amorphous Si film, the poly Si film orthe amorphous/poly-mixed Si film), which makes contact with the first Sifilm 200 e (the homo-epitaxial Si film), may be caused to becomehomo-epitaxial (grow in solid phase epitaxy) and may be changed(modified) to a homo-epitaxial Si film. In other words, the crystalstate of a portion of the second Si film 200 g may be changed to thesame crystal state as the crystal state of the first Si film 200 e. Theregion changed into a homo-epitaxial state may be regarded as a portionof the first Si film 200 e. That is to say, by performing the annealingstep, it is possible to expand the region of the laminated film occupiedby the first Si film 200 e.

[Processing Condition of Annealing Step]

The supply flow rates of the N₂ gas controlled by the MFCs 241 d and 241e are respectively set to fall within a range of e.g., 0 to 10,000 sccm.

The internal pressure of the process chamber 201 may be set at apressure lower than the atmosphere pressure. For example, similar to theparallel seed step or the CVD film forming step, the internal pressureof the process chamber 201 may be set to fall within a range of 1 to1,000 Pa, and in some embodiments, 1 to 100 Pa.

The temperature of the heater 207 is set such that the temperature ofthe wafer 200 becomes a temperature (a third temperature) equal to orhigher than the aforementioned second temperature. Specifically, thetemperature of the heater 207 is set such that the temperature of thewafer 200 becomes a temperature (a third temperature) which falls withina range of, e.g., 500 to 700 degrees C., and in some embodiments, 550 to600 degrees C.

If the temperature of the wafer 200 is less than 500 degrees C., thesolid phase epitaxial growth is difficult to occur. Thus, it issometimes difficult to make homo-epitaxial the portion of the second Sifilm 200 g, which makes contact with the first Si film 200 e. Thisproblem may be solved by setting the temperature of the wafer 200 at 500degrees C. or more. By setting the temperature of the wafer 200 at 550degrees C. or more, it is possible to increase the growth efficiency ofthe solid phase epitaxial growth and to efficiently make homo-epitaxialthe portion of the second Si film 200 g, which makes contact with thefirst Si film 200 e.

If the temperature of the wafer 200 exceeds 700 degrees C., there may bea case where the portion of the second Si film 200 g, which makescontact with the first Si film 200 e, does not become homo-epitaxial butbecomes a poly. This problem may be solved by setting the temperature ofthe wafer 200 at 700 degrees C. or less. By setting the temperature ofthe wafer 200 at 600 degrees C. or less, it becomes easy to allow theportion of the second Si film 200 g, which makes contact with the firstSi film 200 e, to grow in solid phase epitaxy and to becomehomo-epitaxial.

Accordingly, the temperature of the wafer 200 may be set at thetemperature (the third temperature) which falls within a range of, e.g.,500 to 700 degrees C., and in some embodiments, 550 to 600 degrees C. Inthe aforementioned temperature zone, if the temperature of the wafer 200is set at a temperature close to the lower limit temperature, namely ifthe thermal treatment is slowly performed at a temperature close to thelower limit temperature, it is possible to appropriately perform thesolid phase epitaxial growth.

As the inert gas, it may be possible to use an inexpensive and highlysafe gas. In addition to the N₂ gas, it may be possible to use, e.g., anoble gas such as an Ar gas, a He gas, a Ne gas, a Xe gas or the like.

(Purge and Return to Atmospheric Pressure)

If the thermal treatment is completed, the valves 243 d and 243 e areopened. The N, gas is supplied into the process chamber 201 from each ofthe gas supply pipes 232 d and 232 e, and is exhausted through theexhaust pipe 231. The N₂ gas serves as a purge gas. Thus, the interiorof the process chamber 201 is purged with the inert gas, and the gas orthe reaction byproduct remaining within the process chamber 201 isremoved from the interior of the process chamber 201 (purge).Thereafter, the internal atmosphere of the process chamber 201 issubstituted with the inert gas (inert gas substitution), and theinternal pressure of the process chamber 201 is returned to theatmospheric pressure (return to atmospheric pressure).

(Boat Unloading and Wafer Discharge)

The seal cap 219 is moved down by the boat elevator 115 to open thelower end of the reaction tube 203. The processed wafers 200 supportedby the boat 217 are unloaded from the lower end of the reaction tube 203outside of the reaction tube 203 (boat unloading). Thereafter, theprocessed wafers 200 are discharged from the boat 217 (wafer discharge).

(3) Effects According to the Present Embodiment

According to the present embodiment, one or more effects may beachieved, as follows.

(a) At the parallel seed step, by performing Step 1 of supplying the DCSgas containing an halogen element to the wafer 200 having a surface onwhich monocrystalline Si is exposed, it is possible to remove thenatural oxide film 200 b formed on the surface of the monocrystalline Siand to generate dangling bonds of Si on the surface of themonocrystalline Si. This enables the epitaxial Si film (the first Sifilm 200 e) to grow on the monocrystalline Si. Consequently, the filmincluding the first Si film 200 e and the second Si film 200 g laminatedon the first Si film 200 e, namely the laminated film including theepitaxial Si film formed at the side of a lower layer, may be formed onthe surface of the wafer 200 (on the monocrystalline Si). Since thelaminated film includes the epitaxial Si film formed at the side of alower layer, the laminated film becomes a high-quality film which islower in contact resistance with wafer 200 than a Si mono-film composedof only amorphous Si, poly Si or amorphous/poly-mixed Si and which issuperior in electrical characteristic. In the case where ahalogen-element-free silane precursor gas such as a hydrogenated silaneprecursor gas or an aminosilane precursor gas containing an amino groupin one molecule or the like is used in place of the DCS gas, anepitaxial Si film is difficult to grow on the monocrystalline Si. Thismakes it difficult to achieve the aforementioned effect.

(b) At the parallel seed step, by performing Step 1 of supplying the DCSgas containing an halogen element to the wafer 200 having a surface onwhich the insulation film 200 a is exposed, it is possible to form Siadsorption sites on the surface of the insulation film 200 a. This makesit possible to reliably perform the formation of the second seed 200 d,namely the formation of the seed layer 200 f, on the insulation film 200a. Consequently, in the case where a recess is formed on the surface ofthe wafer 200 and the side portion of the recess is configured by theinsulation film 200 a, it is possible to reliably perform the formationof the second Si film 200 g within in the recess, namely the embeddingof the Si film within the recess. Furthermore, it is possible to havethe laminated film (the Si film), which is formed on the wafer 200,become a dense film having no pinhole. It is also possible to have thelaminated film (the Si film) become a film exhibiting a high resistanceto hydrogen fluoride (HF).

(c) At the parallel seed step, by performing Step 1, it is possible toprovide an environment, in which homo-epitaxial growth easily occurs inthe bottom portion of the recess, and to form Si adsorption sites in theside portion and the top portion of the recess. This makes it possibleto start, without delay, the formation of the first Si film 200 e andthe seed layer 200 f on the wafer 200. Consequently, it is possible toshorten the incubation time (delay of growth) of the laminated film (theSi film) and to enhance the productivity of the film forming process.

(d) At the parallel seed step, by alternately performing the supply ofthe DCS gas and the supply of the DS gas, it is possible to increase thedensity of the first seed 200 c and the second seed 200 d and to preventthe first Si film 200 e and the seed layer 200 f from growing in anisland shape. This makes it possible to enhance the step coverage of thefirst Si film 200 e and the seed layer 200 f. Consequently, it ispossible to have the Si film, which is formed on the wafer 200, become adense film having no pinhole. It is also possible to have the Si filmbecome a film exhibiting a high resistance to hydrogen fluoride (HF).

(e) At the parallel seed step, by alternately performing the supply ofthe DCS gas and the supply of the DS gas, it is possible to restrain anexcessive gas phase reaction from being generated within the processchamber 201 and to reduce the amount of particles generated within theprocess chamber 201.

(f) At the parallel seed step and the CVD film forming step, the filmforming efficiency of the finally-formed laminated film and thecharacteristics thereof such as the film thickness uniformity and thelike may be made compatible by using silane precursor gases havingdifferent molecular structures (chemical structures), namely silaneprecursor gases differing in material from each other.

For example, at the parallel seed step, by using, as the second processgas, the DS gas which has two Si atoms in one molecule and which islower in pyrolysis temperature (more easily decomposable) and higher inadsorption efficiency than the MS gas used at the CVD film forming step,it is possible to enhance the generation efficiency of the first seed200 c and the second seed 200 d. This makes it possible to enhance theformation efficiency of the first Si film 200 e and the seed layer 200f. That is to say, by using the DS gas as the second process gas andusing the MS gas as the third process gas, as compared with a case wherethe MS gas is used as the second and third gases, it is possible toenhance the film forming efficiency of the laminated film formed on thewafer 200.

For example, at the CVD film forming step, by using, as the thirdprocess gas, the MS gas which has one Si atom in one molecule and whichis higher in pyrolysis temperature (more hardly decomposable) and lowerin adsorption efficiency than the DS gas used at the parallel seed step,it is possible to appropriately control the deposition rates of thefirst Si film 200 e and the second Si film 200 g. This makes it possibleto improve the characteristics, such as the in-plane film thicknessuniformity, the step coverage and the like, of the first Si film 200 eand the second Si film 200 g. That is to say, by using the DS gas as thesecond process gas and using the MS gas as the third process gas, ascompared with a case where the DS gas is used as the second and thirdgases, it is possible to improve the characteristics, such as thein-plane film thickness uniformity, the step coverage and the like, ofthe laminated film formed on the wafer 200.

By performing the annealing step, it is possible to further improve thequality of the laminated film formed on the wafer 200. For example, theportion of the second Si film 200 g, which makes contact with the firstSi film 200 e, is caused to become homo-epitaxial (grow in solid phaseepitaxy), and the region of the laminated film occupied by the first Sifilm 200 e (the homo-epitaxial Si film) is expanded. This makes itpossible to further reduce the contact resistance of the laminated film.Furthermore, by performing, e.g., the annealing step, it is possible tomake the laminated film denser and to have the laminated film become afilm exhibiting a higher resistance to HF.

(h) The aforementioned effects may be equally achieved even when ahalosilane gas other than the DCS gas is used as the first process gas,a hydrogenated silane gas other than the DS gas is used as the secondprocess gas, a hydrogenated silane gas other than the MS gas is used asthe third process gas, and a dopant gas other than the PH gas is used asthe dopant gas.

(4) Modifications

The film forming sequence according to the present embodiment is notlimited to the form described above and may be modified as in themodifications to be described below.

Modification 1

As can be noted in a film forming sequence illustrated in FIG. 6 or thesubsequent drawings, at the parallel seed step, a step (pre-cleaningstep) of supplying a DCS gas to the wafer 200 may be performed prior tostarting the cycle which alternately performs Steps 1 and 2. Even inthis modification, it is possible to achieve the same effects as thoseachieved in the film forming sequence illustrated in FIG. 4. It is alsopossible to reliably obtain the aforementioned action exercised bysupplying the DCS gas to the wafer 200. Particularly, by making thesupply time of the DCS gas at the pre-cleaning step longer than thesupply time of the DCS gas at Step 1, it is possible to further reliablyobtain the aforementioned action exercised by supplying the DCS gas tothe wafer 200.[DCS→(DCS→DS)×n→M]→ANL

Si

Modification 2

As can be noted in a film forming sequence illustrated in FIG. 7, at theparallel seed step, when the cycle which alternately performs Steps 1and 2 is executed a predetermined number of times, the supply time ofthe DCS gas at Step 1 of the first cycle may be set longer than thesupply time of the DCS gas at Step 1 of the subsequent cycles. Even inthis modification, it is possible to achieve the same effects as thoseachieved in the film forming sequence illustrated in FIG. 4. It is alsopossible to reliably obtain the aforementioned action exercised bysupplying the DCS gas to the wafer 200.

Modification 3

As can be noted in a film forming sequence illustrated in FIG. 8, at theparallel seed step, when the cycle which alternately performs Steps 1and 2 is executed a predetermined number of times, the supply flow rateof the DCS gas at Step 1 of the first cycle may be set larger than thesupply flow rate of the DCS gas at Step 1 of the subsequent cycles. Evenin this modification, it is possible to achieve the same effects asthose achieved in the film forming sequence illustrated in FIG. 4. It isalso possible to reliably obtain the aforementioned action exercised bysupplying the DCS gas to the wafer 200.

Modification 4

As can be noted in a film forming sequence illustrated in FIG. 9, at theparallel seed step, when the cycle which alternately performs Steps 1and 2 is executed a predetermined number of times, the supply flow rateof the DCS gas at Step 1 may be gradually reduced every time the cycleis executed. Furthermore, at the parallel seed step, when the cyclewhich alternately performs Steps 1 and 2 is executed a predeterminednumber of times, the supply time of the DCS gas at Step 1 may begradually shortened every time the cycle is executed. Even in thismodification, it is possible to achieve the same effects as thoseachieved in the film forming sequence illustrated in FIG. 4 and achievedin modifications 1 to 3. In addition, by reducing the supply flow rateor the supply time of the DCS gas during the course of the parallel seedstep, it is possible to reduce the amount of the DCS gas used and toreduce the film forming cost.

Modification 5

As can be noted in a film forming sequence illustrated in FIG. 10 or thesubsequent drawings, at the parallel seed step, after performing Step 1,Step 2 may be intermittently performed a plurality of times. Even inthis modification, it is possible to achieve the same effects as thoseachieved in the film forming sequence illustrated in FIG. 4.Furthermore, by not performing the supply of the DCS gas during thecourse of the parallel seed step, it is possible to reduce the useamount of the DCS gas and to reduce the film forming cost. Moreover, bysetting the supply time of the DCS gas at Step 1 of this modification tobecome longer than the supply time of the DCS gas at Step 1 of the filmforming sequence illustrated in FIG. 4, it is possible to reliablyobtain the aforementioned action exercised by supplying the DCS gas tothe wafer 200. In addition, by setting the supply flow rate of the DCSgas at Step 1 of this modification to become larger than the supply flowrate of the DCS gas at Step 1 of the film forming sequence illustratedin FIG. 4, it is possible to reliably obtain the aforementioned actionexercised by supplying the DCS gas to the wafer 200.[(DCS→DS)×n→MS]→ANL

Si

Modification 6

As can be noted in a film forming sequence illustrated in FIG. 11 or thesubsequent drawings, silane precursor gases having the same molecularstructure, namely silane precursor gases identical in material with eachother, may be used as the second and third process gases. FIG. 11illustrates a case where a DS gas is used as the second and thirdprocess gases. Even in this modification, it is possible to achieve thesame effects as those achieved in the film forming sequence illustratedin FIG. 4. Furthermore, if the DS gas lower in pyrolysis temperature(higher in adsorptivity) than the MS gas is used as the second and thirdprocess gases, it is possible to increase the deposition rate of the Sifilm formed on the wafer 200 and to improve the productivity of the filmforming process. In addition, if the MS gas higher in pyrolysistemperature (lower in adsorptivity) than the DS gas is used as thesecond and third process gases, it is possible to improve the stepcoverage and the film thickness uniformity of the Si film formed on thewafer 200.[(DCS→DS)×n→DS]→ANL

Si

Modification 7

A chlorosilane precursor gas other than the DCS gas may be used as thefirst process gas. Film forming sequences, in which an HCDS gas and anMCS gas are used as the first process gas, are illustrated below.[(HCDS→DS)×n→MS]→ANL

Si[(MCS→DS)×n→MS]→ANL

Si

Even in this modification, it is possible to achieve the same effects asthose achieved in the film forming sequence illustrated in FIG. 4.Furthermore, by using the HCDS gas, which is larger in the number of Clatoms contained in one molecule than the DCS gas, as the first processgas, it is possible to make the aforementioned action exercised bysupplying the DCS gas to the wafer 200 stronger than action available inthe film forming sequence illustrated in FIG. 4. In addition, by usingthe MCS gas, which is smaller in the number of Cl atoms contained in onemolecule than the DCS gas, as the first process gas, it is possible toappropriately suppress the aforementioned action exercised by supplyingthe DCS gas to the wafer 200 so as to become weaker than actionavailable in the film forming sequence illustrated in FIG. 4.

Modification 8

Instead of a carbon (C)-free silane precursor gas, a C-containing silaneprecursor gas, namely a silane precursor gas serving as a C source, maybe used as the first process gas. Film forming sequences, in which a1,1,2,2-tetrachloro-1,2-dimethyldisilane ((CH₃)₂Si₂Cl₄, abbreviation:TCDMDS) gas and a bis(trichlorosilyl)methane ((SiCl₃)₂CH₂, abbreviation:BTCSM) gas are used as the first process gas, are illustrated below.[(TCDMDS→DS)×n→MS]→ANL

Si[(BTCSM→DS)×n→MS]→ANL

Si

Even in this modification, it is possible to achieve the same effects asthose achieved in the film forming sequence illustrated in FIG. 4.Furthermore, according to this modification, it is possible to add asmall amount of C into the first Si film 200 e or the seed layer 200 fformed at the parallel seed step. By adding C into the first Si film 200e, it becomes easy to restrain the first Si film 200 e from becoming apoly and to make the first Si film 200 e become an epitaxial Si film.Furthermore, by adding C into the seed layer 200 f, it is possible toreduce the grain size of crystal grains which constitute the seed layer200 f. It is therefore easy to make the seed layer 200 f become a denselayer. However, depending on the specifications of a device formed onthe wafer 200, there may be a case where it is advisable to avoid theaddition of C into the first Si film 200 e or the seed layer 200 f. Inthis case, similar to the film forming sequence illustrated in FIG. 4, aC-free hydrogenated silane precursor gas may be used as the firstprocess gas.

Modification 9

A halosilane precursor gas which contains a halogen group other than Cl(a chloro group), for example, a halosilane precursor gas which containsF (a fluoro group), Br (bromo group), I (iodine group) or the like, maybe used as the first process gas. As the first process gas, it may bepossible to use, e.g., a fluorosilane precursor gas such as amonofluorosilane (SiH₃F, abbreviation: MFS) gas, a tetrafluorosilane,i.e., silicon tetrafluoride (SiF₄, abbreviation: STF) gas, atrifluorosilane (SiHF₃, abbreviation: TFS) gas, a hexafluorodisilane(Si₂F₆, abbreviation: HFDS) gas or the like, a bromosilane precursor gassuch as a monobromosilane (SiH₃Br, abbreviation: MBS) gas, atetrabromosilane, i.e., silicon tetrabromide (SiBr₄, abbreviation: STB)gas, a tribromosilane (SiHBr3, abbreviation: TBS) gas, ahexabromodisilane (Si₂Br₆, abbreviation: HBDS) gas or the like, and aniodosilane precursor gas such as a monoiodosilane (SiH₃I, abbreviation:MIS) gas, a tetraiodosilane, i.e., silicon tetraiodide (SiI₄,abbreviation: STI) gas, a triiodosilane (SiHI₃, abbreviation: TIS) gas,a hexaiododisilane (Si₂I₆, abbreviation: HIDS) gas or the like. Filmforming sequences, in which an STF gas, an STB gas and an STI gas areused as the first process gas, are illustrated below.[(STF→DS)×n→MS]→ANL

Si[(STB→DS)×n→MS]→ANL

Si[(STI→DS)×n→MS]→ANL

Si

Even in this modification, it is possible to achieve the same effects asthose achieved in the film forming sequence illustrated in FIG. 4.However, if a gas containing F is used as the first process gas, theremay be a case where the film formation base (the surface of themonocrystalline Si or the surface of the insulation film 200 a) ispre-etched. In order to suppress the pre-etching, a halosilane precursorgas containing a halogen group other than F may be used as the firstprocess gas.

Modification 10

A Si-free chloro-based gas containing a chloro group may be used as thefirst process gas. Furthermore, a Si-free halogen-based gas containing ahalogen group other than Cl may be used as the first process gas. Filmforming sequences, in which a hydrogen chloride (HCl) gas, a chlorine(Cl₂) gas, a BCl₃ gas and a chlorine fluoride (ClF₃) gas are used as thefirst process gas, are illustrated below.[(HCl→DS)×n→MS]→ANL

Si[(Cl₂→DS)×n→MS]→ANL

Si[(BCl₃→DS)×n→MS]→ANL

Si[(ClF₃→DS)×nMS]→ANL

Si

Even in this modification, it is possible to achieve the same effects asthose achieved in the film forming sequence illustrated in FIG. 4.However, if a Si-free halogen-based gas is used as the first processgas, there may be a case where the film formation base (the surface ofthe monocrystalline Si or the surface of the insulation film 200 a) ispre-etched. In order to suppress the pre-etching, a halogen-based gascontaining Si, for example, a chlorosilane precursor gas, may be used asthe first process gas.

Modification 11

Not only a C- and nitrogen (N)-free silane precursor gas but also a C-and N-containing silane precursor gas, namely a silane precursor gasserving as a C source and an N source, may be used as the second processgas. As the second process gas, it may be possible to use, e.g., anaminosilane precursor gas such as a monoaminosilane (SiH₃R) gas, adiaminosilane (SiH₂RR′) gas, a triaminosilane (SiHRR′R″) gas, atetraaminosilane (SiRR′R′′R′″) gas or the like. In this regard, each ofR, R′, R″ and R′″ indicates a ligand. As the aminosilane precursor gas,it may be possible to use, e.g., a butyl aminosilane (BAS) gas, abis-tert-butyl amino silane (BTBAS) gas, a dimethyl aminosilane (DMAS)gas, a bis dimethyl aminosilane (BDMAS) gas, a tridimethyl aminosilane(3DMAS) gas, a diethyl aminosilane (DEAS) gas, a bis diethyl aminosilane(BDEAS) gas, a dipropyl aminosilane (DPAS) gas, a diisopropylaminosilane (DIPAS) gas or the like. Film forming sequences, in which aBTBAS gas, a 3DMAS gas and a DIPAS gas are used as the second processgas, are illustrated below.[(HCDS→BTBAS)×n→MS]→ANL

Si[(HCDS→3DMAS)×n→MS]→ANL

Si[(HCDS→DIPAS)×n→MS]→ANL

Si

Even in this modification, it is possible to achieve the same effects asthose achieved in the film forming sequence illustrated in FIG. 4.Furthermore, according to this modification, similar to modification 8,it is possible to add a small amount of C into the first Si film 200 eor the seed layer 200 f formed at the parallel seed step. By doing so,it becomes easy to have the first Si film 200 e grow homo-epitaxially orto make the seed layer 200 f dense. However, depending on thespecifications of a device formed on the wafer 200, there may be a casewhere it is advisable to avoid the addition of C or N into the first Sifilm 200 e or the seed layer 200 f. In this case, similar to the filmforming sequence illustrated in FIG. 4, a C- and N-free hydrogenatedsilane precursor gas may be used as the first process gas.

Other Embodiments of the Present Disclosure

One embodiment of the present disclosure has been specifically describedabove. However, the present disclosure is not limited to theaforementioned embodiment but may be differently modified withoutdeparting from the spirit of the present disclosure.

For example, in the aforementioned embodiment, there has been describeda case where the wafer 200 having the surface structure illustrated inFIG. 12A is processed. However, the present disclosure is not limitedthereto.

For example, as illustrated in FIG. 12B, the present disclosure may besuitably applied to a case where a recess is formed on the surface ofthe wafer 200 and an insulation film 200 a is formed so as to surroundthe opening portion of the recess, namely a case where the bottomportion of the recess is formed of the monocrystalline Si and the sideportion of the recess is formed of the monocrystalline Si and theinsulation film 200 a. Furthermore, for example, as illustrated in FIG.12C, the present disclosure may be suitably applied to a case whererecesses are formed on the surface of the wafer 200 and insulation films200 a are formed so as to fill the recesses. Moreover, for example, asillustrated in FIG. 12D, the present disclosure may be suitably appliedto a case where a recess is formed on the surface of the wafer 200 andinsulation films 200 a are formed in the side portions of the recess.

In either case, by performing the parallel seed step and the CVD filmforming step illustrated in the aforementioned embodiment, it ispossible to have the first Si film 200 e homo-epitaxially grow on themonocrystalline Si and to have the second Si film 200 g grow on theinsulation film 200 a. Thus, a laminated structure (a laminated film)including the first Si film and the second Si film formed on the firstSi film may be formed on the monocrystalline Si. In addition, byperforming the annealing step illustrated in the aforementionedembodiment, it is possible to expand the region of the laminated filmoccupied by the first Si film.

For example, in the aforementioned embodiment, there has been describeda case where the parallel seed step, the CVD film forming step and theannealing step are performed within the same process chamber (in-situ).However, the present disclosure is not limited thereto. As analternative example, the parallel seed step, the CVD film forming stepand the annealing step may be performed within different processchambers (ex-situ). If the series of steps are performed in-situ, thewafer 200 is not exposed to the atmosphere while performing the seriesof steps. It is therefore possible to consistently process the wafer 200while keeping the wafer 200 under a vacuum state. This makes it possibleto stably process a substrate. If some of the steps are performedex-situ, the internal temperatures of the respective process chambersmay be set in advance at, e.g., the processing temperatures required inthe respective steps or the temperatures close to the processingtemperatures. This makes it possible to shorten the time required intemperature adjustment and to enhance the production efficiency.

Further, although, in the aforementioned embodiments, modifications orthe like, for example, there has been described a case where theannealing step is performed after the first Si film and the second Sifilm are formed, the annealing step may be omitted. That is, accordingto the method of the aforementioned embodiments or modifications, it ispossible to form an epitaxial Si film, without performing the annealingstep, i.e., in an as-deposited state on the interface between themonocrystalline Si and the second Si film. Therefore, there is no needfor the annealing step to be necessarily performed in order to obtainsuch configuration (structure). However, even in this case, if theannealing step is performed, it is possible to enlarge the area of theepitaxial film and to further reduce the contact resistance.

The method of the aforementioned embodiments or modifications can beapplied to a manufacturing process for a dynamic random access memory(hereinafter, referred to as “DRAM”) which is a volatile semiconductormemory device (volatile memory). Herein below, description on themanufacturing process for the DRAM will be made with reference to FIGS.15A to 15H and FIGS. 16A to 16G.

Herein, only a part of the manufacturing process for the DRAM will bedescribed for the sake of convenience and description on the remainderof the manufacturing process will be omitted. Further, herein, only apart of the film or structure constituting the DRAM will be describedand description on the remainder of the film or structure will beomitted.

First, as shown in FIG. 15A, a trench is formed on the surface of thewafer by etching the surface of the wafer composed of a monocrystallineSi using an SiO film or an SiN film as a hard mask. After that, as shownin FIG. 15B, an SiO film or the like is formed as a liner film on thesurface of the wafer in which the trench is formed. The SiO film may beformed by, e.g., a CVD method or a thermal oxidation method. Thereafter,as shown in FIG. 15C, the inside of the trench having the liner film onits surface is buried with an SiO film. The SiO film may be forming by,e.g., a CVD method.

After burying the trench, as shown in FIG. 15D, a planarization processis performed on the surface by CMP. After the planarization, as shown inFIG. 15E, the SiO film, the SiN film, and the like formed on the waferare removed by dry etching or the like. After that, as shown in FIG.15F, a liner film is formed again. That is, an SiO film or the like isformed again as a liner film on the surface of the trench. The SiO filmmay be formed by, e.g., a CVD method.

After that, as shown in FIG. 15G, a tungsten film W for the word line isformed on the liner film (SiO film) and the trench is buried with the Wfilm. The W film my be formed by, e.g., a CVD method. After burying theinside of the trench with the W film, a part of the W film (upperportion) is removed by dry etching or the like. FIG. 15G shows a statein which a part of the W film buried in the trench is removed. Afterthat, as shown in FIG. 15H, an SiN film is formed on the W film which isburied in the trench and a part of which is removed. The SiN film may beformed by, e.g., a CVD method. After forming the SiN film, planarizationis performed on the surface by CMP. In this way, it is possible to forma structure in which the W film and the SiN film are laminated in thetrench. FIG. 15H shows a state available after the surface planarizationis performed after the SiN film is formed on the W film in the trench.

Thereafter, as shown in FIG. 16A, interlayer insulation films such as anSiO film, an SiN film or the like are formed. These films may be formedby, e.g., a CVD method. Thereafter, as shown in FIG. 16B, the SiN filmon the SiO film is patterned by lithography, dry etching, and the like.Further, dry etching is performed to the SiO film using the SiN film asa hard mask. In this way, a portion of the SiO film formed on the SiNfilm formed in the trench is allowed to remain while other parts of theSiO film are removed. Therefore, after the dry etching, the SiO film andthe SiN film having served as a hard mask when the SiO film wasdry-etched remain on the SiN film formed in the trench. FIG. 16B shows astate available after the SiO film is dry-etched. After that, as shownin FIG. 16C, the SiN film which served as the hard mask when the SiOfilm was dry-etched is removed by dry etching.

After that, as shown in FIG. 16D, a parallel seed step similar to thatin the embodiments or modifications described above is performed, sothat a first seed layer (a first Si film) formed of a homo-epitaxial Silayer is formed on a portion in which the surface of the wafer isexposed, i.e., on the monocrystalline Si and a second seed layer formedof an amorphous Si layer, a poly Si layer or an amorphous/poly-mixed Silayer is formed on the SiO film. FIG. 16D illustrates a case where ahomo-epitaxial Si (Epi-Si) layer is formed as the first seed layer onthe monocrystalline Si and an amorphous Si (a-Si) layer is formed as thesecond seed layer on the SiO film. In this case, the first seed layermay be referred to as an epitaxial Si seed layer. Further, the secondseed layer may be referred to as an amorphous Si seed layer.

After that, as shown in FIG. 16E, a CVD film forming step similar tothat in the embodiments or modifications described above is performed,so that the first seed layer (the first Si film) on the monocrystallineSi is caused to be additionally grown homo-epitaxially (a homo-epitaxialSi film is additionally grown homo-epitaxially on the first seed layer),while the second Si film formed of an amorphous Si layer, a poly Silayer or an amorphous/poly-mixed Si layer is formed on the second seedlayer on the SiO film. In this way, an inside of a recess defined by theadjacent SiO films and the monocrystalline Si can be buried with the Sifilm. Thus, a laminated structure in which the second Si film is formedon the first Si film can be formed on the monocrystalline Si. That is,an epitaxial Si film can be formed on an interface between themonocrystalline Si and the second Si film. FIG. 16E illustrates a casewhere an epitaxial Si film is formed as the first Si film and anamorphous Si film is formed as the second Si film. That is, FIG. 16Eillustrates a case where an epitaxial Si film is formed on an interfacebetween the monocrystalline Si and the amorphous Si film. Further, inthis case, as in the embodiments or modifications described above, adopant such as P, B, As, or the like may be added to the Si film. Afterthat, it may be possible to perform an annealing step similar to that inthe embodiments or modifications described above so as to enlarge thearea of the epitaxial Si film. Further, according to the method of theaforementioned embodiments or modifications, it is possible to form anepitaxial Si film, without performing the annealing step, i.e., in anas-deposited state, and thus, the annealing step can be omitted. Thefirst Si film and the second Si film serve as a contact plug.

After that, surface planarization is performed by CMP, as shown in FIG.16F. After the surface planarization, as shown in FIG. 16G, a contactpart is formed and, thereafter, a capacitor part is formed. A lowerportion of FIG. 16G illustrates a laminated structure including thecapacitor part and the contact part in a longitudinal sectional view,while the upper portion of FIG. 16G illustrates a portion of thecapacitor part indicated with a broken line in a transverse sectionalview.

In this way, major parts of the DRAM are formed.

Even in a case where the method of the embodiments or modificationsdescribed above is applied to a manufacturing process for the DRAM,contact resistance can be significantly reduced, thereby enabling largeenhancements to the electrical characteristics.

The embodiments or modifications described above can be applied to amanufacturing process for a flash memory which is anon-volatilesemiconductor memory device (non-volatile memory). Herein below, amanufacturing process for a three-dimensional NAND type flash memory(hereinafter, referred to as 3DNAND) among other NAND type flashmemories which are one kind of the flash memory will be described withreference to FIGS. 17A to 17H. The three-dimensional NAND type flashmemory may be simply referred to as a three-dimensional flash memory(three-dimensional non-volatile semiconductor memory device).

Herein, for the sake of convenience, only a part of the manufacturingprocess for the 3DNAND will be described and description on theremainder thereof will be omitted. Further, herein, for the sake ofconvenience, only a part of films or structures constituting the 3DNANDwill be described and description on the remainder thereof will beomitted.

First, as shown in FIG. 17A, a multilayer laminated film (hereinafter,simply referred to as a laminated film) in which an SiN film and an SiOfilm are alternately laminated to form a plurality of layers is formedon the surface of the wafer composed of the monocrystalline Si. Herein,a case where an uppermost layer and a lowermost layer are formed as anSiO film is illustrated. These films may be formed by, e.g., a CVDmethod. Although a case where the lamination number is 9 is shown FIG.17A, the present disclosure is not limited to such a configuration. Forexample, the lamination number may be equal to or higher than 20, andmay be equal to or higher than 30 or equal to or higher than 40.

Thereafter, as shown in FIG. 17B, a channel hole is formed in thelaminated film by dry etching or the like and an insulation film of anONO film, that is, a film formed of three layers of the SiO film/the SiNfilm/the SiO film is formed in the channel hole. These films may beformed by, e.g., a CVD method. FIG. 17B shows a state in which the ONOfilm is formed in the channel hole formed in the laminated film.

As shown in FIG. 17C, a parallel seed step similar to that in theembodiments or modifications described above is performed in a statewhere a portion of the ONO film making contact with the wafer isremoved. In this way, a first seed layer (a first Si film) formed of ahomo-epitaxial Si layer is formed on a portion in which the surface ofthe wafer is exposed, i.e., on the monocrystalline Si and a second seedlayer formed of an amorphous Si layer, a poly Si layer or anamorphous/poly-mixed Si layer is formed on the ONO film (specifically,on the SiO film constituting the ONO film). FIG. 17C illustrates a casewhere a homo-epitaxial Si (Epi-Si) layer is formed as the first seedlayer on the monocrystalline Si and a poly Si (Poly-Si) layer is formedas the second see layer on the SiO film. In this case, the first seedlayer may be referred to as an epitaxial Si seed layer. Further, thesecond seed layer may be referred to as a poly Si seed layer.

After that, as shown in FIG. 17D, a CVD film forming step similar tothat in the embodiments or modifications described above is performed,so that the first seed layer (the first Si film) on the monocrystallineSi is caused to be additionally grown homo-epitaxially (a homo-epitaxialSi film is additionally grown homo-epitaxially on the first seed layer),while the second Si film formed of an amorphous Si layer, a poly Silayer or an amorphous/poly-mixed Si layer is formed on the second seedlayer on the ONO film. FIG. 17D illustrates a case where ahomo-epitaxial Si (Epi-Si) film is formed as the first Si film and apoly Si (Poly-Si) film is formed as the second Si film. That is, FIG.17D illustrates a case where an epitaxial Si film is formed on themonocrystalline Si and a poly Si film is formed on the ONO film.Further, in this case, as in the embodiments or modifications describedabove, a dopant such as P, B, As, or the like may be added to the Sifilm. The film thickness of the Si film may be set to be equal to orless than 10 nm, for example, 3 to 10 nm and may be further set to beequal to or less than 5 nm, for example, 3 to 5 nm. After that, it maybe possible to perform an annealing step similar to that in theembodiments or modifications described above so as to enlarge the areaof the epitaxial Si film. Further, according to the method of theaforementioned embodiments or modifications, it is possible to form anepitaxial Si film, without performing the annealing step, i.e., in anas-deposited state, and thus, the annealing step can be omitted. Thefirst Si film and the second Si film serve as a channel. Herein below,these Si films (the first Si film, the second Si film) functioning as achannel may be referred to as a channel Si.

After that, as shown in FIG. 17E, an inside of a recess defined byremaining portions in the channel hole, i.e., the first Si film (anepitaxial Si film) and the second Si film (a poly Si film) is buriedwith an SiO film. The SiO film may be formed by, e.g., a CVD method.

In this way, the channel part is formed.

After that, as shown in FIG. 17F, a trench is formed in the multilayerlaminated film (a laminated film) in which the SiN film and the SiO filmare alternately laminated to form the plurality of layers. The trenchcan be formed by dry etching or the like. Thereafter, the SiN filmconstituting the laminated film is removed by dry etching or the like.As a result, the SiO film constituting the laminated film remains. FIG.17F illustrates a state where the SiN film was removed by dry etching orthe like after the forming of the trench.

In this state, as shown in FIG. 17G, metal films such as a TiN film, a Wfilm, or the like, which serve as a control gate, are formed in aportion from which the SiN film is removed, i.e., a portion between thevertically adjacent SiO films. These films may be formed by, e.g., a CVDmethod. After that, the metal films or the like such as the TiN film,the W film, or the like which are formed in the trench (protruding fromthe portion between the vertically adjacent SiO films) during the filmforming process are removed by dry etching or the like. In this way, thetrench is formed again. FIG. 17G illustrates a state available after thetrench is formed again.

In this way, a control gate part in which the SiO film and the controlgate (the TiN film, the W film or the like) are laminated with eachother is forming.

In this state, as shown in FIG. 17H, the inside of the trench is buriedwith an SiO film or the like. The SiO film may be formed by, e.g., a CVDmethod. In this case, the SiO film is also formed in upper portions ofthe control gate part and the channel part. After that, a contact holeis formed in the upper portion of the channel part and a metal filmserving as a contact is formed within the contact hole. FIG. 17Hillustrates a state available after the metal film is formed within thecontact hole.

In this way, major parts of the 3DNAND are formed.

Even in a case where the method of the embodiments or modificationsdescribed above is applied to a manufacturing process for the 3DNAND,contact resistance of the Si wafer and the channel Si can besignificantly reduced, thereby enabling large enhancements to theelectrical characteristics.

Further, by applying the method of the embodiments or modificationsdescribed above to the manufacturing process for the 3DNAND, flat anddense seed layers (the first seed layer, the second seed layer) can beformed and thin but flat and dense Si films (the first Si film, thesecond Si film) can be formed, so that an Si film without having a pinhole (a pin hole-free film) can be obtained. Thus, it is possible toprevent a base film of the Si film from being etched in a wet etchingprocess using HF or the like which is performed after the forming of theSi film. Further, since the thin but flat and dense Si film can beformed, the second Si film (the poly Si film) can be thinned, so thatthe charge trap density in the crystal grain boundary can be reduced andthe electron mobility to the channels of the 3DNAND can be increased.

Recipes (e.g., programs describing processing procedures and processingconditions) used in the substrate processing may be preparedindividually (in a plural number) according to the process contents(e.g., the kind, composition ratio, quality, film thickness, processingprocedure and processing condition of the film to be formed) and may bestored in the memory device 121 c via a telecommunication line or theexternal memory device 123. Moreover, at the start of the process, theCPU 121 a may properly select an appropriate recipe from the recipesstored in the memory device 121 c according to the substrate processingcontents. This enables a single substrate processing apparatus to formfilms of different kinds, composition ratios, qualities and thicknesseswith enhanced reproducibility. In addition, this configuration makes itpossible to reduce an operator's burden (e.g., a burden borne by anoperator when inputting processing procedures and processing conditions)and to quickly start the process while avoiding an operation error.

The recipes mentioned above are not limited to newly-prepared ones butmay be prepared by, for example, modifying the existing recipes alreadyinstalled in the substrate processing apparatus. When modifying therecipes, the modified recipes may be installed in the substrateprocessing apparatus via a telecommunication line or a recording mediumstoring the recipes. In addition, the existing recipes already installedin the substrate processing apparatus may be directly modified byoperating the input/output device 122 of the substrate processingapparatus.

In the aforementioned embodiment, there has been described an example inwhich films are forming using a batch type substrate processingapparatus capable of processing a plurality of substrates at a time. Thepresent disclosure is not limited to the aforementioned embodiment butmay be appropriately applied to, e.g., a case where films are formedusing a single-substrate-type substrate processing apparatus capable ofprocessing a single substrate or several substrates at a time. Inaddition, in the aforementioned embodiment, there has been described anexample in which films are formed using a substrate processing apparatusprovided with a hot-wall-type processing furnace. The present disclosureis not limited to the aforementioned embodiment but may be appropriatelyapplied to a case where films are formed using a substrate processingapparatus provided with a cold-wall-type processing furnace. In thesecases, the processing procedures and the processing conditions may besimilar to, e.g., those of the aforementioned embodiment.

The present disclosure may be suitably applied to, e.g., a case where afilm is formed using a substrate processing apparatus provided with aprocessing furnace 302 illustrated in FIG. 14A. The processing furnace302 includes a process vessel 303 which defines a process chamber 301, ashower head 303 s as a gas supply part configured to supply a gas intothe process chamber 301 in a shower-like manner, a support table 317configured to horizontally support one or more wafers 200, a rotaryshaft 355 configured to support the support table 317 from below, and aheater 307 installed in the support table 317. Gas supply ports 332 aand 332 b are connected to inlets (gas introduction holes) of the showerhead 303 s. Gas supply systems similar to the first process gas supplysystem and the dopant gas supply system of the above-describedembodiment are connected to the gas supply port 332 a. Gas supplysystems similar to the second process gas supply system and the thirdprocess gas supply system of the above-described embodiment areconnected to the gas supply port 332 b. A gas distribution plateconfigured to supply a gas into the process chamber 301 in a shower-likemanner is installed in outlets (gas discharge holes) of the shower head303 s. The shower head 303 s is installed at such a position as to facethe surfaces of the wafers 200 carried into the process chamber 301. Anexhaust port 331 configured to evacuate the interior of the processchamber 301 is installed in the process vessel 303. An exhaust systemsimilar to the exhaust system of the above-described embodiment isconnected to the exhaust port 331.

In addition, the present disclosure may be suitably applied to, e.g., acase where a film is formed using a substrate processing apparatusprovided with a processing furnace 402 illustrated in FIG. 14B. Theprocessing furnace 402 includes a process vessel 403 which defines aprocess chamber 401, a support table 417 configured to horizontallysupport one or more wafers 200, a rotary shaft 455 configured to supportthe support table 417 from below, a lamp heater 407 configured toirradiate light toward the wafers 200 disposed within the process vessel403, and a quartz window 403 w which transmits the light irradiated fromthe lamp heater 407. Gas supply ports 432 a and 432 b are connected tothe process vessel 403. Gas supply systems similar to the first processgas supply system and the dopant gas supply system of theabove-described embodiment are connected to the gas supply port 432 a.Gas supply systems similar to the second process gas supply system andthe third process gas supply system of the above-described embodimentare connected to the gas supply port 432 b. The gas supply ports 432 aand 432 b are respectively formed at the lateral side of the endportions of the wafers 200 carried into the process chamber 401, namelyat such positions as not to face the surfaces of the wafers 200 carriedinto the process chamber 401. An exhaust port 431 configured to evacuatethe interior of the process chamber 401 is formed in the process vessel403. An exhaust system similar to the exhaust system of theabove-described embodiment is connected to the exhaust port 431.

In the case of using these substrate processing apparatuses, it ispossible to perform film formation by the same sequences and processingconditions as those of the embodiments and modifications describedabove. It is also possible to achieve the same effects as those achievedin the embodiments and modifications described above.

The embodiments and modifications described above may be appropriatelycombined with one another. In addition, the processing conditions usedat this time may be similar to, e.g., the processing conditions of theembodiments described above.

EXAMPLE

Next, descriptions will be made on experimental results that support theeffects achieved in the embodiments and modifications described above.

As Sample 1, using the substrate processing apparatus of theabove-described embodiments and according to the film forming sequenceillustrated in FIG. 4, a Si film was formed on a Si wafer having asurface on which monocrystalline Si (a Si wafer surface) and aninsulation film (SiO₂) are exposed, namely on a Si wafer having asurface on which a recess is formed, the recess including a bottomportion formed of the monocrystalline Si and a side portion and a topportion respectively formed of the insulation film. A DCS gas was usedas a first process gas. A DS gas was used as a second process gas. An MSgas was used as a third process gas. The temperature of the Si wafer ata parallel seed step was set to fall within a range of 370 to 390degrees C. The temperature of the Si wafer at a CVD film forming stepwas set to fall within a range of 400 to 500 degrees C. Other processingconditions were set to fall within a range of the processing conditionsdescribed in the aforementioned embodiments.

As Sample 2, using the substrate processing apparatus of theabove-described embodiments and according to the processing proceduressimilar to those of the CVD film forming step of the above-describedembodiments, a Si film was formed on a Si wafer having a surface onwhich monocrystalline Si and an insulation film (SiO₂) are exposed. InSample 2, a parallel seed step was not performed. An MS gas was used asa third process gas. Processing conditions were similar to those of theCVD film forming step used in producing Sample 1.

The cross-sectional structures of the Si films of Samples 1 and 2 wereobserved using a TEM. FIG. 13A is a TEM image illustrating thecross-sectional structure of the Si film of Sample 1, and FIG. 13B is aTEM image illustrating the cross-sectional structure of the Si film ofSample 2.

According to FIG. 13A, it can be appreciated that a laminated structureincluding an epitaxial Si film (an Epi-Si film) and an amorphous Si film(an a-Si film) laminated on the epitaxial Si film is formed on themonocrystalline Si (within the recess). Presumably, this is because thenatural oxide film formed on the surface of the monocrystalline Si wasremoved by performing the parallel seed step when producing Sample 1.That is to say, this is because the formation of the Si film was startedafter desorbing O from the surface of the Si wafer (the surface of themonocrystalline Si) and then providing an environment in whichhomo-epitaxial growth is easy to occur.

According to FIG. 13B, it can be appreciated that an epitaxial Si filmdid not grow on the monocrystalline Si (within the recess) and only anamorphous Si film (an a-Si film) grew on the monocrystalline Si (withinthe recess). The reasons for this appear to be as follows. Since theparallel seed step was not performed when producing Sample 2, thenatural oxide film is not removed from the surface of themonocrystalline Si. O remains in the interface between the surface(monocrystalline Si) of the Si wafer and the Si film. Thus, there is notprovided an environment in which Si grows homo-epitaxially.

As a result of evaluation of the electrical characteristics of the Sifilms formed in Samples 1 and 2, it was confirmed that the Si filmformed in Sample 1 is a high-quality film which is lower in contactresistance than the Si film formed in Sample 2 and superior inelectrical characteristic to the Si film formed in Sample 2. As a resultof thermally treating the Si film (the laminated film) formed in Sample1 under the processing procedures and the processing conditions similarto those of the annealing step illustrated in the above-describedembodiments, it was confirmed that it is possible to expand the regionof the Si film (the laminated film) occupied by the epitaxial Si filmand to further improve the electrical characteristics of the Si film.

Aspects of Present Disclosure

Hereinafter, the preferred aspects of the present disclosure will beadditionally stated.

(Supplementary Note 1)

According to one aspect of the present disclosure, there is provided athree-dimensional flash memory, a dynamic random access memory, or asemiconductor device, including:

a substrate formed of monocrystalline silicon;

an insulation film formed on a surface of the substrate;

a first silicon film formed on the monocrystalline silicon by beinghomo-epitaxially grown using the monocrystalline silicon as a base; and

a second silicon film formed on the insulation film and being differentin crystal structure from the first silicon film.

(Supplementary Note 2)

In the three-dimensional flash memory, the dynamic random access memory,or the semiconductor device of Supplementary Note 1, a recess may beformed on the surface of the substrate, the recess including a bottomportion formed of the monocrystalline silicon and a side portion formedof the insulation film. The first silicon film and the second siliconfilm in the three-dimensional flash memory serve as a channel. The firstsilicon film and the second silicon film in the dynamic random accessmemory serve as a contact plug.

(Supplementary Note 3)

In the three-dimensional flash memory, the dynamic random access memory,or the semiconductor device of Supplementary Note 1 or 2, the firstsilicon film and the second silicon film may be formed by alternatelyperforming supplying a first process gas containing silicon and ahalogen element to the substrate having a surface on which themonocrystalline silicon and the insulation film are exposed andsupplying a second process gas containing silicon and not containing ahalogen element to the substrate, and supplying a third process gascontaining silicon to the substrate.

(Supplementary Note 4)

According to another aspect of the present disclosure, there is provideda method of manufacturing a semiconductor device or a substrateprocessing method, including alternately performing supplying a firstprocess gas containing silicon and a halogen element to a substratehaving a surface on which monocrystalline silicon and an insulation filmare exposed and supplying a second process gas containing silicon andnot containing a halogen element to the substrate; and

supplying a third process gas containing silicon to the substrate,

whereby a first silicon film is homo-epitaxially grown on themonocrystalline silicon and a second silicon film differing in crystalstructure from the first silicon film is grown on the insulation film.

(Supplementary Note 5)

In the method of Supplementary Note 4, in the act of alternatelyperforming the act of supplying the first process gas and the act ofsupplying the second process gas, the first silicon film may behomo-epitaxially grown on the monocrystalline silicon and a seed layermay be formed on the insulation film, and

in the act of supplying the third process gas, the first silicon filmmay be further homo-epitaxially grown and the second silicon film may begrown on the seed layer.

(Supplementary Note 6)

In the method of Supplementary Note 4 or 5, a recess may be formed onthe surface of the substrate, the recess including a bottom portionformed of the monocrystalline silicon and aside portion formed of theinsulation film.

(Supplementary Note 7)

In the method of Supplementary Note 6, a top portion of the firstsilicon film may be covered with the second silicon film grown from theside portion of the recess, so as to stop homo-epitaxial growth of thefirst silicon film.

(Supplementary Note 8)

In the method of Supplementary Note 6 or 7, a top portion of the firstsilicon film may be covered with the second silicon film grown from theside portion of the recess, so as to form a laminated structure (alaminated film) including the first silicon film and the second siliconfilm laminated on the first silicon film.

(Supplementary Note 9)

In the method of any one of Supplementary Notes 4 to 8, a crystalstructure of the second silicon film may be an amorphous, a poly (apolycrystal) or a mixture of the amorphous and the poly. That is to say,the second silicon film may be an amorphous silicon film, a poly siliconfilm or an amorphous/poly-mixed silicon film.

(Supplementary Note 10)

In the method of any one of Supplementary Notes 4 to 9, the firstprocess gas may include silane chloride (compound), the second processgas may include hydrogenated silane (compound), and the third processgas may include hydrogenated silane (compound).

(Supplementary Note 11)

In the method of any one of Supplementary Notes 4 to 10, in the act ofsupplying the third process gas, a dopant gas together with the thirdprocess gas may be supplied to the substrate.

(Supplementary Note 12)

In the method of any one of Supplementary Notes 4 to 11, the secondprocess gas may differ in molecular structure (chemical structure) fromthe third process gas. That is to say, the second process gas may differin material from the third process gas.

(Supplementary Note 13)

In the method of any one of Supplementary Notes 4 to 12, a pyrolysistemperature of the second process gas may be lower than a pyrolysistemperature of the third process gas.

(Supplementary Note 14)

In the method of any one of Supplementary Notes 4 to 11, the secondprocess gas may be identical in molecular structure (chemical structure)with the third process gas. That is to say, the second process gas maybe identical in material with the third process gas.

(Supplementary Note 15)

The method of any one of Supplementary Notes 4 to 14 may further includethermally treating (annealing) the first silicon film and the secondsilicon film.

(Supplementary Note 16)

In the method of Supplementary Note 15, in the act of thermally treatingthe first silicon film and the second silicon film, a portion of thesecond silicon film which makes contact with the first silicon film(homo-epitaxial silicon film) may be changed into a homo-epitaxialstate.

(Supplementary Note 17)

In the method of Supplementary Note 15 or 16, in the act of thermallytreating the first silicon film and the second silicon film, a portionof the second silicon film which makes contact with the first siliconfilm (homo-epitaxial silicon film) may be changed into a homo-epitaxialsilicon film.

(Supplementary Note 18)

In the method of any one of Supplementary Notes 15 to 17, in the act ofthermally treating the first silicon film and the second silicon film, aregion occupied by the first silicon film may be expanded.

(Supplementary Note 19)

In the method of any one of Supplementary Notes 4 to 18, in the act ofalternately performing the act of supplying the first process gas andthe act of supplying the second process gas, a temperature of thesubstrate may be set at a first temperature, and

in the act of supplying the third process gas, a temperature of thesubstrate may be set at a second temperature equal to or higher than thefirst temperature.

(Supplementary Note 20)

In the method of Supplementary Note 19, in the act of thermally treatingthe first silicon film and the second silicon film, a temperature of thesubstrate may be set at a third temperature equal to or higher than thesecond temperature.

(Supplementary Note 21)

According to another aspect of the present disclosure, there is provideda method of manufacturing a semiconductor device or a substrateprocessing method, including alternately performing supplying a firstprocess gas containing a halogen element to a substrate having a surfaceon which monocrystalline silicon and an insulation film are exposed andsupplying a second process gas containing silicon and not containing ahalogen element to the substrate; and

supplying a third process gas containing silicon to the substrate,

whereby a first silicon film is homo-epitaxially grown on themonocrystalline silicon and a second silicon film differing in crystalstructure from the first silicon film is grown on the insulation film.

(Supplementary Note 22)

According to another aspect of the present disclosure, there is provideda substrate processing apparatus, including:

a process chamber configured to accommodate a substrate therein;

a first process gas supply system configured to supply a first processgas containing silicon and a halogen element to the substrate existingwithin the process chamber;

a second process gas supply system configured to supply a second processgas containing silicon and not containing a halogen element to thesubstrate existing within the process chamber;

a third process gas supply system configured to supply a third processgas containing silicon to the substrate existing within the processchamber;

a heater configured to heat the substrate existing within the processchamber; and

a control part configured to control the first process gas supplysystem, the second process gas supply system, the third process gassupply system and the heater so as to perform processes of alternatelyperforming supplying the first process gas to the substrate having asurface on which monocrystalline silicon and an insulation film areexposed and supplying the second process gas to the substrate, andsupplying the third process gas to the substrate, whereby a firstsilicon film is homo-epitaxially grown on the monocrystalline siliconand a second silicon film differing in crystal structure from the firstsilicon film is grown on the insulation film.

(Supplementary Note 23)

According to another aspect of the present disclosure, there is provideda gas supply system including:

a first gas supply part configured to supply a first process gascontaining silicon and a halogen element to a substrate;

a second gas supply part configured to supply a second process gascontaining silicon and not containing a halogen element to thesubstrate; and

a third gas supply part configured to supply a third process gascontaining silicon to the substrate,

wherein the first gas supply part, the second gas supply part and thethird gas supply part are controlled so as to perform processes ofalternately performing supplying the first process gas to the substratehaving a surface on which monocrystalline silicon and an insulation filmare exposed and supplying the second process gas to the substrate, andsupplying the third process gas to the substrate, whereby a firstsilicon film is homo-epitaxially grown on the monocrystalline siliconand a second silicon film differing in crystal structure from the firstsilicon film is grown on the insulation film.

(Supplementary Note 24)

According to another aspect of the present disclosure, there is provideda program or a non-transitory computer-readable recording medium storingthe program, wherein the program is configured to cause a computer toperform processes of alternately performing supplying a first processgas containing silicon and a halogen element to a substrate having asurface on which monocrystalline silicon and an insulation film areexposed and supplying a second process gas containing silicon and notcontaining a halogen element to the substrate; and

supplying a third process gas containing silicon to the substrate,

whereby a first silicon film is homo-epitaxially grown on themonocrystalline silicon and a second silicon film differing in crystalstructure from the first silicon film is grown on the insulation film.

According to the present disclosure, it is possible to improve thequality of a Si film formed on a substrate on which monocrystalline Siand an insulation film are exposed.

While certain embodiments have been described, these embodiments havebeen presented by way of example only, and are not intended to limit thescope of the disclosures. Indeed, the novel methods and apparatusesdescribed herein may be embodied in a variety of other forms;furthermore, various omissions, substitutions and changes in the form ofthe embodiments described herein may be made without departing from thespirit of the disclosures. The accompanying claims and their equivalentsare intended to cover such forms or modifications as would fall withinthe scope and spirit of the disclosures.

What is claimed is:
 1. A method of manufacturing a semiconductor device, comprising: alternately performing supplying a first process gas containing silicon and a halogen element to a substrate having a surface on which monocrystalline silicon and an insulation film are exposed and supplying a second process gas containing silicon and not containing a halogen element to the substrate; and supplying a third process gas containing silicon to the substrate, whereby a first silicon film is homo-epitaxially grown on the monocrystalline silicon and a second silicon film differing in crystal structure from the first silicon film is grown on the insulation film.
 2. The method of claim 1, wherein in the act of alternately performing the act of supplying the first process gas and the act of supplying the second process gas, the first silicon film is homo-epitaxially grown on the monocrystalline silicon and a seed layer is formed on the insulation film, and in the act of supplying the third process gas, the first silicon film is further homo-epitaxially grown and the second silicon film is grown on the seed layer.
 3. The method of claim 1, wherein a recess is formed on the surface of the substrate, the recess including a bottom portion formed of the monocrystalline silicon and a side portion formed of the insulation film.
 4. The method of claim 3, wherein a top portion of the first silicon film is covered with the second silicon film grown from the side portion of the recess, so as to stop homo-epitaxial growth of the first silicon film.
 5. The method of claim 3, wherein a top portion of the first silicon film is covered with the second silicon film grown from the side portion of the recess, so as to form a laminated structure including the first silicon film and the second silicon film laminated on the first silicon film.
 6. The method of claim 1, wherein a crystal structure of the second silicon film is an amorphous, a polycrystal or a mixture of the amorphous and the polycrystal.
 7. The method of claim 1, wherein the first process gas includes silane chloride, the second process gas includes hydrogenated silane, and the third process gas includes hydrogenated silane.
 8. The method of claim 1, wherein in the act of supplying the third process gas, a dopant gas together with the third process gas is supplied to the substrate.
 9. The method of claim 1, wherein the second process gas differs in molecular structure from the third process gas.
 10. The method of claim 1, wherein a pyrolysis temperature of the second process gas is lower than a pyrolysis temperature of the third process gas.
 11. The method of claim 1, wherein the second process gas is identical in molecular structure with the third process gas.
 12. The method of claim 1, further comprising thermally treating the first silicon film and the second silicon film.
 13. The method of claim 12, wherein in the act of thermally treating the first silicon film and the second silicon film, a portion of the second silicon film which makes contact with the first silicon film is changed into a homo-epitaxial state.
 14. The method of claim 12, wherein in the act of thermally treating the first silicon film and the second silicon film, a portion of the second silicon film which makes contact with the first silicon film is changed into a homo-epitaxial silicon film.
 15. The method of claim 12, wherein in the act of thermally treating the first silicon film and the second silicon film, a region occupied by the first silicon film is expanded.
 16. The method of claim 1, wherein in the act of alternately performing the act of supplying the first process gas and the act of supplying the second process gas, a temperature of the substrate is set at a first temperature, and in the act of supplying the third process gas, a temperature of the substrate is set at a second temperature equal to or higher than the first temperature.
 17. The method of claim 16, further comprising thermally treating the first silicon film and the second silicon film, wherein in the act of thermally treating the first silicon film and the second silicon film, a temperature of the substrate is set at a third temperature equal to or higher than the second temperature.
 18. The method of claim 1, wherein the semiconductor device includes a three-dimensional flash memory or a dynamic random access memory.
 19. A non-transitory computer-readable recording medium storing a program that causes a computer to perform processes of alternately performing supplying a first process gas containing silicon and a halogen element to a substrate having a surface on which monocrystalline silicon and an insulation film are exposed and supplying a second process gas containing silicon and not containing a halogen element to the substrate; and supplying a third process gas containing silicon to the substrate, whereby a first silicon film is homo-epitaxially grown on the monocrystalline silicon and a second silicon film differing in crystal structure from the first silicon film is grown on the insulation film. 